Union of India - Act
The Environment (Protection) Rules, 1986
UNION OF INDIA
India
India
The Environment (Protection) Rules, 1986
Rule THE-ENVIRONMENT-PROTECTION-RULES-1986 of 1986
- Published on 19 November 1986
- Commenced on 19 November 1986
- [This is the version of this document from 19 November 1986.]
- [Note: The original publication document is not available and this content could not be verified.]
1. Short title and commencement. - (i) These rules may be called The Environment (Protection) Rules, 1986.
2. Definitions. - In these rules, unless the context otherwise requires,-
3. Standards for emission or discharge of environmental pollutants. - (1) For the purposes of protecting and improving the quality of the environment and preventing and abating environmental pollution, the standards for emission or discharge of environmental pollutants from the industries, operations or processes shall be as specified in [Schedules I to IV].
[* * *] [ Proviso omitted by S.O. 23(E), dated 16.1.1991 (w.e.f. 16.1.1991).]4. Directions. - (1) Any direction issued under section 5 shall be in writing.
5. Prohibition and restriction on the location of industries and the carrying on processes and operations in different areas. - (1) The Central Government may take into consideration the following factors while prohibiting or restricting the location of industries and carrying on of processes and operations in different areas:-
(i)Standards for quality of environment in its various aspects laid down for an area.(ii)The maximum allowable limits of concentration of various environmental pollutants (including noise) for an area.(iii)The likely emission or discharge of environmental pollutants from an industry, process or operation proposed to be prohibited or restricted.(iv)The topographic and climatic features of an area.(v)The biological diversity of the area which, in the opinion of the Central Government, needs to be preserved.(vi)Environmentally compatible land use.(vii)Net adverse environmental impact likely to be caused by an industry, process or operation proposed to be prohibited or restricted.(viii)Proximity to a protected area under the Ancient Monuments and Archaeological Sites and Remains Act, 1958 or a sanctuary, National Park, game reserve or closed area notified, as such under the Wild Life (Protection) Act, 1972, or places protected under any treaty, agreement or convention with any other country or countries or in pursuance of any decision made in any international conference, association or other body.(ix)Proximity to human settlements.(x)Any other factor as may be considered by the Central Government to be relevant to the protection of the environment in an area.6. [ Procedure for taking samples.
- The Central Government or the officer empowered to take samples under section 11 shall collect the sample in sufficient quantity to be divided into two uniform parts and effectively seal and suitably mark the same and permit the person from whom the sample is taken to add his own seal or mark to all or any of the portions so sealed and marked. In case where the sample is made up in containers or small volumes and is likely to deteriorate or be otherwise damaged if exposed, the Central Government or the officer empowered shall take two of the said samples without opening the containers and suitably seal and mark the same. The Central Government or the officer empowered shall dispose of the samples so collected as follows:-7. Service of notice. - The Central Government or the officer empowered shall serve on the occupier or his agent or person in charge of the place a notice then and there in Form I of his intention to have the sample analysed.
8. Procedure for submission of samples for analysis, and the form of laboratory report thereon. - (1) Sample taken for analysis shall be sent by the Central Government or the officer empowered to the environmental laboratory by registered post or through special messenger alongwith Form II.
9. Functions of environmental laboratories. - The following shall be the functions of environmental laboratories:-
10. Qualifications of Government Analyst. - A person shall not be qualified for appointment or recognised as a Government Analyst unless he is a -
11. Manner of giving notice. - The manner of giving notice under clause (b) of section 19 shall be as follows, namely:-
12. [ Furnishing of information to authorities and agencies in certain cases.
- Where the discharge of environmental pollutant in excess of the prescribed standard occurs or is apprehended to occur due to any accident or other unforeseen act or event, the person in charge of the place at which such discharge occurs or is apprehended to occur shall forthwith intimate the fact of such occurrence or apprehension of such occurrence to all the following authorities or agencies, namely:-13. [ Prohibition and restriction on the handling of hazardous substances in different areas.
14. [ Submission of environment statement.
- Every person carrying on an industry, operation or process requiring consent under section 25 of the Water (Prevention and Control of Pollution) Act, 1974 (6 of 1974) or under section 21 of the Air (Prevention and Control of Pollution) Act, 1981 (14 of 1981) or both or authorisation under the Hazardous Wastes (Management and Handling) Rules, 1989 issued under the Environment (Protection) Act, 1986 (29 of 1986) shall submit an environmental [statement] [for the financial year ending on the 31st March in Form V to the concerned State Pollution Control Board on or before the [thirtieth day of September] [Inserted by G.S.R. 329(E), dated 13.10.1992 (w.e.f. 13.3.1992).][every year, beginning 1993.] [Inserted by G.S.R. 329(E), dated 13.10.1992 (w.e.f. 13.3.1992).][I] [Schedule renumbered as Schedule I by S.O. 82(E), dated 16-2-1987 (w.e.f. 16-2-1987). ]
(See rule 3)| Sl. No. | Industry | Parameter | Standards |
| 1 | 2 | 3 | 4 |
| 1. | Caustic soda industry | Concentration not to exceed, milligramme per litre (except for pH and flow) | |
| Total concentration of mercury in the final effluent* | 0.01 | ||
| Mercury bearing waste-water generation (flow) | 10 kilolitres/tonne of caustic soda produced | ||
| pH | 5.5- 9.0 | ||
| *Final effluent is the combined effluent from (a) cell house, (b) brine plant, (c) chlorine handling, (d)hydrogen handling, (e) hydrochloric acid plant | |||
| 2. | Man-made fibres(synthetic) | Concentration not to exceed, milligramme per litre (except for pH) | |
| Suspended solids | 100 | ||
| [BOD (3 days at 27 [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).][°]C)] | 30 | ||
| Petroleum Oil refinery | pH | 5.5-9.0 | |
| 3. [] [Substituted by G.S.R. 186(E), dated 18-3-2008 (w.e.f. 18-3-2008).] | [A.Effluent] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| [Limiting value for concentration (mg/I except for pH)] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | |||
| 1. [ pH] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 6. [0-8.5] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 2. [ Oil & Grease] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 5. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 3. [ BOD3days, 27°C] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 15. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 4. [ COD] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 125. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 5. [ Suspended Solids] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 20. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 6. [ Phenols] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [35] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 7. [ Sulphide] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [5] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 8. [ CN] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [20] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 9. [ Ammonia as N] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 15. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 10. [ TKN] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 40. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 11. [ P] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 3. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 12. [ Cr (Hexavalent)] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [1] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 13. [ Cr (Total)] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 2. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 14. [ Pb] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [1] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 15. [ Hg] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [01] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 16. [ Zn] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 5. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 17. [ Ni] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 1. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 18. [ Cu] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 1. [0] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 19. [ V] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [2] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 20. [ Benzene] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [1] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| 21. [ Benzo(a)-Pyrene] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | 0. [2] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | ||
| [Notes. - ] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | |||
| (i) [Concentration limits shall be complied with at the outlet, discharging effluent (excluding discharge from sea water cooling systems) to receiving environment (surface water bodies, marine systems or public sewers). In case of application of treated effluent directly for irrigation/horticulture purposes (within or outside the premises of refinery), make-up water for cooling systems, fire fighting, etc., the concentration limits shall also be complied with at the outlet before taking the effluent for such application.However, any use in the process such as use of sour water in desolater is excluded for the purpose of compliance.] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | |||
| (ii) [ In case of circulating seawater cooling, the blow-down from cooling systems shall be monitored for pH and oil& grease (also hexavalent & total chromium, if chromate treatment is given to cooling water) and shall conform to the concentration limits for these parameters. In case of reuse of treated effluent as cooling water make-up, all the parameters (as applicable for treated effluent) shall be monitored and conform to the prescribed standards.] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] | |||
| (iii) [ In case of once through cooling with seawater, the oil & grease content in the effluent from cooling water shall not exceed 1.0 mg/1] [Substituted by Notification No. G.S.R. 186 (E) dated 18.3.2008 (w.e.f. 19.11.1986)] |
| [B. Emissions | ||||
| Limiting concentration in mg/Nm, unless stated | ||||
| Fuel Type | Existing refineries | New Refinery/Furnace/Boiler | ||
| (Furnace, Boiler and captive Power Plant) | SulphurDioxide (SO2) | Gas | 50 | 50 |
| Liquid | 1700 | 850 | ||
| Oxides of Nitrogen (NOx) | Gas | 350 | 250 | |
| Liquid | 450 | 350 | ||
| Particulate Matter (PM) | Gas | 10 | 5 | |
| Liquid | 100 | 50 | ||
| Carbon Monoxide (CO) | Gas | 150 | 100 | |
| Liquid | 200 | 150 | ||
| Nickel and Vanadium (Ni+V) | Liquid | 5 | 5 | |
| Hydrogen Sulphide(H2S) in fuel gas | Liquid/gas | 150 | 150 | |
| Sulphurcontent in liquid fuel, weight % | Liquid/gas | 1.0 | 0.5 | |
| Notes. - | ||||
| (i) In case of mixed fuel (gas and liquid) use, the limit shall be computed based on heat supplied by gas and liquid fuels. | ||||
| (ii) All the furnaces/boilers with heat input of 10 million kilo calories/hour or more shall have continuous systems for monitoring of SO2, and NOx. Manual monitoring for all the emission parameters in such furnaces or boilers shall be carried out once in two months. | ||||
| (iii) All the emission parameters in furnaces/boilers having heat input less than 10million kilo calories/hour will be monitored once in three months. | ||||
| (iv) In case of continuous monitoring, one hourly average concentration values shall be complied with 98% of the time in a month. Any concentration value obtained through manual monitoring, if exceeds the limiting concentration value, shall be considered as non-compliance. | ||||
| (v) Data on Nickel and Vanadium content in the liquid fuel (in ppm)shall be reported. Nickel and Vanadium in the liquid fuel shall be monitored at least once in six months, if liquid fuel source quality are not changed. In case of changes, measurement is necessary after every change. |
| (FCC Regenerators) | Limiting concentration in mg/Nm³, unless stated | ||
| Existing refineries hydro-processed FCC feed | Other than hydro-processed FCC feed | New Refinery/FCC Commissioned | |
| SulphurDioxide (SO2) | 500 | 1700 | 500(for hydro-processed feed) 850 (for other feed) |
| Oxides of Nitrogen (NOx) | 400 | 450 | 350 |
| Particulate Matter (PM) | 100 | 100 | 50 |
| Carbon Monoxide (CO) | 400 | 400 | 300 |
| Nickel and Vanadium(Ni+V) | 2 | 5 | 2 |
| Opacity, % | 30 | 30 | 30 |
| Notes. - | |||
| (i) In case part feed is hydro-processed, the emission values shall be calculated proportional to the feed rates of untreated and treated feeds. | |||
| (ii) FCC regenerators shall have continuous systems for monitoring of SO2 and NOx. One hourly average concentration values shall be complied with 98% of the time in a month, in case of continuous monitoring. Manual monitoring for all the emission parameters shall be carried out once in two months. | |||
| (iii) Any concentration value obtained through manual monitoring, if exceeds the limiting concentration value, shall he considered as non-compliance. | |||
| (iv) Data onSulphur(weight in %), Nickel (PPM) and Vanadium (PPM) content in the feed to FCC shall be reported regularly. | |||
| (v) Limit of Carbon Monoxide emissions shall be complied with except during annual shut down of CO boiler for statutory maintenance. |
| Plant capacity | Existing SRU | New SRU or Refinery Commissioned | ||
| (Tonnes/day) | ||||
| [Sulphur recovery Units (SRU)] | Sulphurrecovery, % | Above 20 | 98.7 | 99.5 |
| H2S mg/Nm3, | 15 | 10 | ||
| Sulphurrecovery, % | 5-20 | 96 | 98 | |
| Sulphurrecovery, % | 1-5 | 94 | 96 | |
| Oxides of Nitrogen NOx), mg/Nm3 | Allcapacity | 350 | 250 | |
| Carbon Monoxide (CO), mg/Nm3 | All capacity | 150 | 100 | |
| Notes. - | ||||
| (i)Sulphurrecovery units having capacity above 20 tonnes per day shall have continuous systems for monitoring of SO2. Manual monitoring for all the emission parameters shall be carried out once in a month. | ||||
| (ii) Data on Sulphur Dioxide emissions (mg/Nm3) shall he reported regularly. | ||||
| (iii)Sulphurrecovery efficiency shall be calculated on monthly basis, using quantity of sulphur in the feed to SRU and quantity of sulphur recovered. |
| 1 | 2 | 3 | 4 |
| Emission control for Road Tank Truck/Rail Tank Wagon Loading | |||
| Loading of Volatile Products | Gasoline and Naphtha: | ||
| (i) VOC reduction, % | (i) | 99.5 | |
| (ii) Emission, gm/m3 | (ii) | 5 | |
| Benzene: | |||
| (i) VOC reduction, % | (i) | 99.99 | |
| (ii) Emission, mg/m3 | (ii) | 20 | |
| Toluee/Xylene: | |||
| (i) VOC reduction, % | (i) | 99.98 | |
| (ii) Emission, mg/m3 | (ii) | 150 | |
| Note. - | |||
| (i) It shall be applicable for Gasoline, Naphtha, Benzene, Toluene and Xylene loading. | |||
| (ii) Road Tank Truck shall have Bottom loading and Rail Tank Wagon shall have Top submerged loading. | |||
| (iii) Annual leak testing for vapour collection shall be done. |
| Component | General Hydrocarbon (ppm) | Benzene (ppm) | ||
| Till 31st Dec., 2008 | w.e.f. January 01, 2009 | Till 31st Dec., 2008 | w.e.f. January01, 2009 | |
| Pump/Compressor | 10000 | 5000 | 3000 | 2000 |
| Valves/Flanges | 10000 | 3000 | 2000 | 1000 |
| sOther components | 10000 | 3000 | 2000 | 1000 |
| (7)Monitoring Requirements and Repair Schedule:Following frequency of monitoring of leaks and schedule for repair of leaks shall be followed: | ||
| Component | Frequency of monitoring | Repair schedule |
| Quarterly(semiannual after two consecutive periods with 2% leaks and annual after 5 periods with 2% leaks) | Repair will be started within 5 working days and shall be completed within 15 working days after detection of leak for general hydrocarbons. In case of benzene, the leak shall be attended immediately for repair. | |
| Pump seals | Quarterly | |
| Compressor seals | Quarterly | |
| Pressure relief devices | Quarterly | |
| Pressure relief devices (after venting) | Within 24 hours | |
| Heat Exchangers | Quarterly | |
| Process drains | Annually | |
| Components that are difficult to monitor | Annually | |
| Pump seals with visible liquid dripping | Immediately | Immediately |
| Any component with visible leaks | Immediately | Immediately |
| Any component after repair/replacement | Within five days |
| 4. [ Sugar industry [Substituted by Notification No. G.S.R. 35(E), dated 14.1.2016 (w.e.f. 19.11.1986).] | Effluents | All concentration values are in milligramme per litre except for pH |
| pH | 5.5 - 8.5 | |
| Total Suspended Solids (TSS), milligramme per litre | 100 (for disposal on land)30 (for disposal in surface waters) | |
| Biological Oxygen Demand, BOD [3 days at 270C], milligramme per litre | 30 (for disposal in surface waters) | |
| Oil Grease milligramme per litre | 10 | |
| Total Dissolved Solids (TDS), milligramme per litre | 2100 | |
| Final waste-water discharge limit | 200 litre per tonne of cane crushed | |
| (Final treated effluent discharge restricted to 100 litre per tonne of cane crushed and Wast water from spray pond overflow or cooling tower blow down to be restricted to 100 litre per tonne of cane crushed and only single outlet point form unit is allowed.) | ||
| Emissions | ||
| The particulate matter emissions from the stack shall be less than 150 milligramme per normal cubic metre] |
4.
| S.N | Soil Texture | Loading rate in m3/Ha/Day |
| 1 | Sandy | 225 to 280 |
| 2 | Sandy loam | 170 to 225 |
| 3 | Loam | 110 to 170 |
| 4 | Clay loam | 55 to 110 |
| 5 | Clay | 35 to 55 |
1. Establishment of cooling arrangement and polishing tank for recycling the excess condensate water to process or utilities or allied units.
2. Effluent Treatment Plant to be stabilized one month prior to the start of the crushing season and continue to operate one month after the crushing season.
3. During no demand period for irrigation, the treated effluent to be stored in a seepage proof lined pond having 15 days holding capacity only.
4. Flow meter to be installed in all water abstraction points and usage of fresh water to be minimized.
5. Suitable Air pollution control devices to be installed to meet the particulate matter emission standard.
| 5.Thermal power plants | Maximum,limiting concentration, milligramme per litre (except for pH andtemperature) | |
| Condensercooling waters | pH | 6.5- 8.5 |
| (oncethrough cooling system) | Temperature | Notmore than 5°C higher than the intake water temperature |
| Freeavailable chlorine | 0.5 | |
| Boilerblowdowns | Suspendedsolids | 100 |
| Oiland grease | 20 | |
| Copper(total) | 1.0 | |
| Iron(total) | 1.0 | |
| Coolingtower blowdown | Freeavailable chlorine | 0.5 |
| Zinc | 1.0 | |
| Chromium(total) | 0.2 | |
| Phosphate | 5.0 | |
| Othercorrosion inhibiting material | Limitto be established on case by case basis by Central Board in caseof Union territories and State Boards in case of States | |
| Ashpond effluent | pH | 6.5- 8.5 |
| Suspendedsolids | 100 | |
| Oiland grease | 20 |
| S.No. | Industry | Parameter | Standard(applicablefor all modes of disposal*) |
| 1 | 2 | 3 | 4 |
| 6 | AllIntegrated textile units, units of Cotton/ Woollen/ Carpets/Polyester, Units having Printing/ Dyeing/ Bleaching process ormanufacturing and Garment units. | TREATEDEFFLUENTS | Maximumconcentration values in mg/l except for pH, colour, and SAR |
| pH | 6.5to 8.5 | ||
| SuspendedSolids | 100 | ||
| Colour,P.C.U. (Platinum Cobalt Units) | 150 | ||
| Bio-ChemicalOxygen DemoC](BOD3) | 30 | ||
| Oiland Grease | 10 | ||
| ChemicalOxygen Demand (COD) | 250 | ||
| TotalChromium as (Cr) | 2.0 | ||
| Sulphide(as S) | 2.0 | ||
| PhenolicCompounds (as C6H5OH) | 1.0 | ||
| TotalDissolved Solids, Inorganic (TDS) | 2100** | ||
| SodiumAbsorption Ratio (SAR) | 26** | ||
| AmmonicalNitrogen (as N) | 50 |
1. *In case of direct disposal into rivers and lakes, the Central Pollution Control Board (CPCB) or State Pollution Control Boards/ Pollution Control Committees (SPCBs/ PCCs) may specify more stringent standards depending upon the quality of the recipient system.
2. **Standards for TDS and SAR shall not be applicable in case of marine disposal through proper marine outfall.
3. The treated effluent shall be allowed to be discharged in the ambient environment only after exhausting options for reuse in industrial process/ irrigation in order to minimise freshwater usage.
4. Any textile unit attached with the Common Effluent Treatment Plant (CETP) shall achieve the inlet and treated effluent quality standards as specified in serial number 55 of Schedule-I to the Environment (Protection) Rules, 1986 and shall also be jointly and severally responsible for ensuring compliance.
5. The standalone Micro, Small and Medium Enterprises (MSMEs) as per the MSME Development Act, 2006 shall meet the values specified above.
6. The standalone large scale units shall meet the values specified above; however, CPCB or SPCBs/ PCCs with the approval of CPCB, may mandate Zero Liquid Discharge in Large scale units in environmentally sensitive/ critical areas.
7. The TDS value with respect to treated effluent shall be 2100 milligramme per litre; however, in case where TDS in intake water is above 1100 milligramme per litre, a maximum contribution up to 1000 milligramme per litre shall be permitted provided the maximum value of 3100 milligramme per litre is not exceeded in the treated effluent.]
The special parameters are to be stipulated by the Central Board in case of Union territories State Boards in case of States depending upon the dye used in the industry. Where the industry uses chrome dyes. sulphur dyes and or phenolic compounds in the dyeing/ printing process, the limits on chromium of 2 mg/litre, sulphides of 2 mg/litre, and phenolic compounds of 5 mg/litre, respectively shall be imposed.Where the quality requirement of the recipient system so warrants, the limit of BOD should be lowered upto 30 according to the requirement by the State Boards for the States and the Central Board for the Union territories.A limit on sodium absorption ratio of 26 should be imposed by the State Boards for the the Central Board for the Union territories if the disposal of the effluent is to be made on land.| 7. Composite woolen mills | Concentration not to exceed, milligramme per litre(except for pH and bio-assay) | |
| Common: | ||
| Suspended solids | 100 | |
| PH | 5.5 - 9.0 | |
| [BOD (3 days at 27ºC)] [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | 100 | |
| Oil and grease | 10 | |
| Bio-assay | 90% survival of fish after 96 hours | |
| Special: | ||
| Total chromium (as Cr) | 2 | |
| Sulphide(as S) | 2 | |
| PhenolicCompounds (as C6H5OH) | 5 |
| Sl.No. | Industry | Parameter | Standards |
| 1 | 2 | 3 | 4 |
| Sl.No. | Industry | Parameter | Standard |
| (1) | (2) | (3) | (4) |
| 8 | Dye and DyeIntermediate Industry | A.Emission Standards (Process) | |
| Limitingconcentration in milligramme/Normal cubic metre (mg/Nm3), unlessotherwise stated | |||
| Oxides of Sulphur( SOx) | 200 | ||
| HCl (Acid Mist) | 35 | ||
| Ammonia (NH3) | 30 | ||
| Chlorine (Cl2) | 15 | ||
| Note:Allprocess vents shall have chimney height of atleast two metresabove the shed or building where equipment is installed. | |||
| B. Effluent Standards | |||
| Limitingconcentration not to exceed in milligramme/litre (mg/l), exceptfor pH, Temperature, Colour and Bioassay. | |||
| disposal insurface water | marine disposa | on land forirrigation | |
| pH | 6.0 to 8.5 | 5.5 – 9.0 | 5.5 – 9.0 |
| Suspended Solids | 100 | - | 200 |
| BiochemicalOxygen Demand - BOD (3 days, 27°C) | 30 | 100 | 100 |
| Chemical OxygenDemand (COD) | 250 | 250 | - |
| AmmonicalNitrogen as N | 50 | 50 | - |
| Temperature | shall not exceed5°C above the receiving water | - | |
| Colour (Hazenunit) | 400 | - | - |
| Mercury (Hg) | 0.01 | 0.01 | - |
| HexavalentChromium (Cr+6) 0.1 | 0.1 | 1.0 | - |
| Total Chromium(Cr) | 2.0 | 2.0 | - |
| Copper (Cu) | 2.0 | 3.0 | - |
| Zinc (Zn) | 5.0 | 15.0 | - |
| Nickel (Ni) | 3.0 | 5.0 | - |
| Lead (Pb) | 0.1 | 2.0 | - |
| Manganese (Mn) | 2.0 | 2.0 | - |
| Cadmium (Cd) | 0.2 | 2.0 | - |
| Chloride (Cl-) | 1000 | - | - |
| Sulphate(SO42-) | 1000 | - | - |
| Phenolic Compoundsas C6H5OH | 1.0 | 5.0 | - |
| Oil Grease | 10.0 | 10.0 | 10.0 |
| Bio-assay Test(with 1:8 dilution of effluents) | 90% survival ofTest animals after 96 hours* in 100% effluent | - | - |
| *The Bioassay test shall be conducted as per IS: 6582: 1971.Note:(i)In case of disposal of effluent on land by industry directly orthrough a CETP, the industry or, CETP as the case may be, shallbe required to install piezometers for monitoring of groundwater.Atleast, two piezometers for three hectares shall be installedfor a plot size above 10 hectares with a minimum of 16piezometers. It shall be one per hectare within a minimum of sixpiezometers for a plot of size smaller than 10 hectares, inconsultation with the concerned State Pollution Control Board forsiting of piezometers.(ii) The standards for Chloride andSulphate shall be applicable only for discharge of treatedeffluent into inland surface water courses. However, whendischarged on land for irrigation, the norms for Chloride shallnot be more than 600 mg/l over and above the contents of rawwater and the Sodium Absorption Ratio (SAR) shall not exceed26.(iii) Treated /untreated effluent shall be stored inholding tank(s) in such a manner which would not cause pollutionof groundwater. | |||
| C.Emission Standards for Captive Incinerator | |||
| Limitingconcentration in mg/Nm3, unless otherwise stated | SamplingDuration in minutes unless otherwise stated | ||
| Paticulate Matter | 50 | 30or more (for sampling of 300 litres of emission) | |
| HCl (Acid Mist) | 50 | 30 | |
| SO2 | 200 | 30 | |
| Carbon Monoxide | 100 | dailyaverage | |
| Total OrganicCarbon | 20 | 30 | |
| Total Dioxins AndFurans | 0.1ng TEQ/Nm3 | 8hours | |
| Sb+As+Pb+Cr+Co+Cu+Mn+Ni+V+Cd+Th+Hg and their compounds | 1.5 | 2hours | |
| Note:i.All monitored values shall be corrected to 11% oxygen on drybasis.ii. The CO2 concentration in tail gas shall not be lessthan 7%.iii.In case, halogenated organic waste is less than 1% by weight ininput waste,all the facilities in twin chamber incineratorshall be designed so as to achieve a minimum temperature of 850 ±25oC in primary chamber and 950oC in secondary combustion chamberand with a gas residence time in secondary combustion chamber notless than two seconds.orAllthe facilities in single chamber incinerator for gaseoushazardous waste shall be designed so as to achieve a minimumtemperature of 950 oC in the combustion chamber with a gasresidence time not less than two seconds.iv.In case halogenated organic waste is more than 1% by weight ininput waste, waste shall be incinerated only in twin chamberincinerators and all the facilities shall be designed to achievea minimum temperature of 850± 25oC in primary chamber and1100 oC in secondary combustion chamber with a gas residence timein secondary combustion chamber not less than two seconds.v.Scrubber meant for scrubbing emissions from incinerator shall notbe used as quencher.vi.Incineration plants shall be operated, (i.e., combustionchambers) with such temperature, retention time and turbulence,as to achieve Total Organic Carbon (TOC) content in theincineration ash and residue less than 3%, and the loss onignition for ash and residue is less than 5% of the dry weight.In case of non-conformity, ash and residue, as the case may beshall be re-incinerated.vii. Theincinerator shall have a chimney of at least thirty metresheight. | |||
| D.Effluent Standards for Incinerator | |||
| Note:(i)Effluent from scrubber (s) and floor washing shall flow throughclosed conduit or pipe network and be treated to comply with theeffluent standards mention at ‘B’ above.(ii) The built upin Total Dissolved Soilds (TDS) in wastewater of floor washingsshall not exceed 1000 mg/l over and above the TDS of raw waterused. | |||
| E.Stormwater | |||
| Note:(i)Stormwater shall not be allowed to mix with scrubber water and/orfloor washings.(ii)Stormwater shall be channelized through separate drains passingthrough a HDPE lined pit having holding capacity of 10 minutes(hourly average) of rainfall.”. |
| [S.No. [ Substituted by Notification No. G.S.R. 266 (E) dated 30.3.2012 (w.e.f. 19.11.1986)] | Industry | Parameter | Standard |
| (1) | (2) | (3) | (4) |
| 9 | Electroplating,Anodizing Industry | A-EffluentStandards | |
| LimitingConcentration in mg/l, except for pH and Temperature | |||
| (i) CompulsoryParameters | |||
| pH | 6.0 to 9.0 | ||
| Temperature | Shall not exceed5°C above the ambient temperature of the receiving body | ||
| Oil and Grease | 10 | ||
| Suspended Solids | 100 | ||
| Total Metal* | 10 | ||
| Trichloroethane | 0.1 | ||
| Trichloroethane | 0.1 | ||
| (ii) SpecificParameter as per process | |||
| a.Nickel and Chrome plating | |||
| AmmonicalNitrogen, as N | 50 | ||
| Nickle, as Ni | |||
| HexavalentChrommium, as Cr | 0.1 | ||
| Total Chromium, asCr | 2 | ||
| Sulphides, as S | 2 | ||
| Sulphates, as SO4-2 | 400 | ||
| Phosphates, as P | 5 | ||
| Copper as Cu | 3 | ||
| b.Zinc plating | |||
| Cyandies, (as CN-) | 0.2 | ||
| AmmonicalNitrogen, as N | 50 | ||
| Total ResidualChlorine, as Cl | 1 | ||
| HexavalentChromium, as Cr | 0.1 | ||
| Total Chromium, asCr | 2 | ||
| Zinc, as ZN | 5 | ||
| Lead, as Pb | 0.1 | ||
| Iron, as Fe | 3 | ||
| c.Cadmium plating | |||
| Cyanides, (as CN-) | 0.2 | ||
| AmmonicalNitrogen, as N | 50 | ||
| Total ResidualChlorine, as Cl | 1 | ||
| HexavalentChromium, as Cr | 0.1 | ||
| Total Chromium, asCd | 2 | ||
| Cadmium, as Cd | 2 | ||
| d.Anodizing | |||
| AmmonicalNitrogen, as N | 50 | ||
| Total ResidualChlorine, as Cl | 1 | ||
| Aluminium | 5 | ||
| Flourides, as F | 15 | ||
| Sulphates, as SO42- | 400 | ||
| Phosphates, as P | 5 | ||
| e.Copper, Tin plating | |||
| Cyanides, (as CN-) | 0.2 | ||
| Cooper, as Cu | 3 | ||
| Tin | 2 | ||
| f.Precious Metal plating | |||
| Cyanides. (as CN-) | 0.2 | ||
| Total ResidualChlorine, as Cl | 1 | ||
| B.-EmissionStandards+ | |||
| Limitingconcentration in mg/m3 unless stated | |||
| (i)Compulsory parameters | |||
| Acid mist (HCIH2 SO4)** | 50 | ||
| (ii)Specific parameters as per process | |||
| a.Nickle Chromium plating | |||
| Nickle** | 5 | ||
| HexavalentChromium** | 0.5 | ||
| b.Zinc, Cooper or Cadmium plating | |||
| Lead** | 10 | ||
| Cyanides,(Total)** | 5 | ||
| * 'Total Metal'shall account for combined concentration ofZn+Cu+Ni+Al+Fe+Cr+Cd+Pd+Sn+Ag in the effluent.+ Emissionstandards shall be applicable to electroplating units havingwater consumption atleast 5 m3/day. These units shall channelizetheir emission through a stack or chimney having height at least10 metres above ground level or 3 metres above top of shed orbuilding of the unit, whichever is more.** The existing unitsshall comply with the norms of asterisked pollutants by 1stJanuary 2013. However, new units shall comply with the norms witheffect from commissioning of plant. | |||
| C.Stormwater | |||
| Note :(i)Stormwater for a unit (having plot size atleast 200 squaremetres) shall not be allowed to mix with scrubber water, effluentand/or floor washings.(ii) Stormwater within the batterylimits of a unit shall be channelized through separate drain/pipepassing through a High Density Polyethlene (HDPE) lined pithaving holding capacity of ten minutes (Hourly average) ofrainfall.] |
| [S. No. | Industry | Parameter | Standards |
| (1) | (2) | (3) | (4) |
| 10. | Cement Plant (without co processing), Standalone ClinkerGrinding Plant or, Blending Plant | A – Emission Standards | |
| (i) Rotary Kiln –without co processing | |||
| Date of Commissioning | Location | Concentration not to exceed, in mg/Nm3 | |
| (a) | (b) | (c) | |
| Sulphur Dioxide (SO2) in mg/ Nm3 | Irrespective of date of commissioning | Anywhere in the country | 100, 700 and 1000 when pyritic sulphur in the limestone isless than 0.25%, 0.25 to 0.5% and more than 0.5% respectively. |
| Oxides of Nitrogen (NOx) in mg/ Nm3 | After the date of notification (25.8.2014) | Anywhere in the country | (1) 600 |
| Before the date of notification (25.8.2014) | Anywhere in the country | (2) 800 for rotary kiln with InLine Calciner (ILC) technology.(3) 1000 for rotary kiln using mixed stream of ILC, SeparateLine Calciner (SLC) and suspension preheater technology or SLCtechnology alone or without calciner. |
| [S. No. | Industry | Parameter | Standards |
| (1) | (2) | (3) | (4) |
| 10A. | Cement Plant with coprocessing of wastes | A- Emission Standards | |
| Rotary Kiln - with co-processing of Wastes | |||
| Date of Commissioning | Location | Concentration not to exceed, in mg/ Nm3 | |
| (a) | (b) | (c) | |
| Particulate Matter (PM)* | on or after the date of notification (25.8.2014) | anywhere in the country | 30 |
| before the date of notification (25.8.2014) | critically polluted area or urban centres with populationabove 1.0 lakh or within its periphery of 5.0 kilometer radius | 30 | |
| other than critically polluted area or urban centres | 30 | ||
| SO2* | irrespective of date of commissioning | anywhere in the country | 100, 700 and 1000 when pyritic sulphur in the limestone isless than 0.25%, 0.25 to 0.5% and more than 0.5% respectively. |
| NOx* | After the date of notification (25.8.2014) | anywhere in the country | (1) 600 |
| Before the date of notification | anywhere in the country (25.8.2014) | (2) 800 for rotary kiln with InLine Calciner (ILC) technology.(3) 1000 for rotary kiln using mixed stream of ILC, SeparateLine Calciner (SLC) and suspension pre-heater technology or SLCtechnology alone or without calciner. | |
| HCl | 10 mg/ Nm3 | ||
| HF | 1 mg/Nm3 | ||
| TOC | 10 mg/ Nm3** | ||
| Hg and its compounds | 0.05 mg/ Nm3 | ||
| Cd + Tl and their compounds | 0.05 mg/ Nm3 | ||
| Sb + As + Pb + Co + Cr + Cu + Mn + Ni + V andtheir compounds | 0.5 mg/ Nm3 | ||
| Dioxins and Furans | 0.1 ngTEQ/ Nm3 | ||
| Note:The abbreviations usedin the Table shall mean as under: SO2- Sulphurdioxide; NOX- Oxides of Nitrogen; HCl - HydrogenChloride; HF - Hydrogen Flouride; TOC - Total Organic Carbon; Hg- Mercury; Cd - Cadmium; Tl - Thallium; Sb - Antimony; As -Arsenic; Pb - Lead; Co - Cobalt; Cr - Chromium; Cu - Copper; Mn -Manganese; Ni - Nickel; and V - Vanadium.* The concentration values andtimeline for implementation in respect of PM, SO2 and NOx shallbe governed in accordance with the provisions under notificationpublished vide GSR No. 612 (E), dated the 25thAugust,2014 and amended from time to time.** Permitting authority mayprescribe separate standards on case to case basis, if TotalOrganic Carbon (TOC) does not result from the co-processing ofwaste.The height of each individualstack connected to Kiln, Clinker Cooler, Cement Mill, Coal Mill,Raw Mill, Packaging section, etc. shall be of a minimum of 30metres or, as per the formula H = 14 (Q1)0.3and H =74 (Q2)0.27whichever is more, where “H”is the height of stack in metres and “Q1” is themaximum quantity of SO2expected to be emitted inkg/hr and “Q2” is the maximum quantity of PMexpected to be emitted in tonnes/hr through the stack at 100percent rated capacity of the plant;The monitored values of SO2,NOx, HCl, HF, TOC, Metals and Dioxins and Furans atmain kiln stack shall be corrected to 10% Oxygen, on dry basisand the norms for SO2, NOx, HCl, HF, TOC,Metals and Dioxins and Furans shall be applicable to main kilnstack and the norms for Particulate Matter (PM) shall beapplicable to all the stacks in the plant. PM, SO2,NOxshall be monitored continuously. HCl, HF, TOC,Metals and Dioxins and Furans shall be monitored once in a year;Scrubber meant for scrubbing emissions shall not be usedas quencher and plants having separate stack for gaseousemission for the scrubbing unit, the height of this stack shallbe at least equal to the main stack. | |||
| B - Service wastewater (with co-processing of wastes)All efforts shall be made by the industry for 'zero discharge'of service wastewater and in case, the industry prefers todischarge service wastewater, the following norms shall becomplied with: | |||
| Concentration not to exceed, milligram per litre (except pHand temperature) | |||
| pH | 5.5 to 9.0 | ||
| Suspended Solids | 100 | ||
| Oil and Grease | 10 | ||
| Temperature | not more than 5°C higher than the intakewater temperature | ||
| C - Storm waterStorm-water shall not beallowed to mix with effluent, treated sewage, scrubber water andor or floor washings.Storm-water within battery limits of industry shall bechannelized through separate drain(s).] |
| 11. Stone crushingunit] | Suspendedparticulate matter | Thesuspended particulate matter measured between 3 metres and 10metres from any process equipment of a stone crushing unit shallnot exceed 600 micro-grammes per cubic metre. | ||
| [* * *] | ||||
| 13. [ [Substituted by Notification No. G.S.R. 221 (E) dated 18.3.2011 (w.e.f. 19.11.1986)] | RubberProcessing and Rubber Product Industry | A.Effluent Standards (i) Natural Rubber Processing : Centrifugingand Creaming Units | ||
| Limitingvalue for concentration in mg/l, except for pH | ||||
| Inland SurfaceWater | Land forIrrigation Public Sewar | |||
| pH | 6.0-8.5 | 6.0-8.5 | ||
| Suspended Solids | 100 | 200 | ||
| BOD, 3 days at27°C | 30 | 100 | ||
| COD | 250 | - | ||
| Oil and Grease | 10 | 10 | ||
| Total KjeldahiNitrogen, as N | 100 | * | ||
| Free Ammonia | 5 | * | ||
| AmmonicalNitrogen, as N | 50 | * | ||
| Sulphides, as S | 2 | * | ||
| Total DissolvedSolids | 2100 | 2100 | ||
| (ii)Natural Rubber Processing : Craps and Crumb Units | ||||
| pH | 6.0-8.5 | 6.0-8.5 | ||
| Suspended Solids | 100 | * | ||
| Colour | Colourless | * | ||
| Odour | Absent | * | ||
| BOD, 3 days at27°C | 30 | 100 | ||
| COD | 250 | * | ||
| Oil and Grease | 10 | 10 | ||
| Total KjeldahiNitrogen, as N | 50 | * | ||
| AmmonicalNitrogen, as N | 25 | * | ||
| Sulphides, as S | 2 | * | ||
| Total DissolvedSolids | 2100 | 2100 | ||
| (iii)Rubber Products (Moulded, Extruded orCalendared/Fabricated/Rubber Reclamation Unit Latex based Unit) | ||||
| pH | 6.2-8.5 | 6.0-8.5 | ||
| Suspended Solids | 50 | 100 | ||
| Oil and Grease | 10 | 10 | ||
| BOD, 3 days at27°C | 50 | * | ||
| Lead* | 0.1 | * | ||
| Zinc as Zn* | 5 | * | ||
| Total Chromium | 0-05 | * | ||
| (iv)Tyre and Tube Industry | ||||
| pH | 6.0-8.5 | 6.0-8.5 | ||
| Suspended Solids | 50 | * | ||
| Oil and Grease | 10 | 10 | ||
| (v)Synthetic Rubber Industry | ||||
| pH | 6.0-8.5 | 6.0-8.5 | ||
| Colour | Absent | * | ||
| Odour | Absent | * | ||
| BOD, 3 days at27°C | 50 | * | ||
| COD | 250 | * | ||
| Oil and Grease | 10 | 10 | ||
| *Norms for theseparameters shall be prescribed by the concerned State PollutionControl Board/Pollution Control Committee on case basis. | ||||
| B. EmissionStandards* (Rubber Product Industry i.e. Moulded, Extruded orCalendared/Fabricated/Rubber Reclamation Unit/Latex based Unit) | ||||
| Concentration notto exceed in mg/Nm3 | ||||
| Particulate Matter | 150 | |||
| Volatile OrganicCompounds | 50 | |||
| *These emissionstandards shall not be applicable to SSI units. | ||||
| NOTE : | ||||
| Allrubber units shall channelize their fugitive emission through astack having height of 12 metres or 2 metres above roof top ofshed/building whichever is more.] | ||||
| 14. Small Pulp andPaper Industry | Concentration notto exceed milligramme per litre (except for pH and sodiumabsorption ratio) | |||
| *Discharge intoinland surface water Disposal on land | pH | 5.5–9.0 | ||
| Suspended solids | 100 | |||
| BOD | 30 | |||
| pH | 5.5–9.0 | |||
| Suspended solids | 100 | |||
| BOD | 100 | |||
| Sodium AbsorptionRatio | 26 | |||
| [AbsorbableOrganic Halogens (AOX) in effluent discharge [Inserted by Notification No. G.S.R. 546(E), dated 30.8.2005 (w.e.f. 19.11.1986).] | 3.00kg/ton of paper produced with effect from the date of publicationof this notification2.00 kg/ton of paper produced with effectfrom the 1st day of March, 2006;] |
| 15. Fermentation Industry (Distilleries, Maltries and Breweries) | Concentration in the effluent not to exceed milligramme per litre (except for pH and colour and odour) | |
| pH | 5.5 - 9.0 | |
| Colourand odour | [All efforts should be made to remove colour and unpleasant odour as far as practicable. | |
| Suspended solids | 100 | |
| [BOD (3 days at 27 [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).]°C)] | ||
| - Disposal into inland surface water/river/streams | 30mg1 | |
| - Disposal on land or for irrigation | 100 mg/1.] |
| 16. LeatherTanneries | Concentration inthe effluent not to exceed milligramme per litre (except for pHand per cent sodium) | ||||
| InlandSurface Waters | PublicSewers | Landfor Irrigation | MarineCoastal Areas | ||
| (a) | (b) | (c) | (d) | ||
| Suspended Solids | 100 | 600 | 200 | 100 | |
| [BOD (3 days at27ºC)] | 30 | 350 | 100 | 100 | |
| pH | 6.0-9.0 | 6.0-9.0 | 6.0-9.0 | 6.0-9.0 | |
| Chlorides (as Cl) | 1000 | 1000 | 600 | - | |
| Hexavalent | 0.1 | 0.2 | 0.1 | 1.0 | |
| Chromium (Cr+6) | 2.0 | 2.0 | 2.0 | 2.0 | |
| Total Chromium (asCr) | |||||
| Sulphides (as S) | 2.0 | 5.0 | - | 5.0 | |
| Sodium per cent | - | 60 | 60 | - | |
| Boron (as B) | 2.0 | 2.0 | 2.0 | - | |
| Oil and grease | 10 | 20 | 10 | 20 |
| 17. [ [Substituted by Notification No. G.S.R. 1607(E), dated 29.12.2017 (w.e.f. 19.11.1986).] | Fertilizer Industry | A .- Effluent Standards |
| (i) Straight Nitrogenous FertilizerPlant/Ammonia (Urea Plant), Calcium Ammonium Nitrate and AmmoniumNitrate Fertilizers | ||
| Limiting concentration not to exceed inmilligram/litre (mg/l), except for pH | ||
| pH | 6.5 to 8.5 | |
| Suspended Solids | 100 | |
| Oil and Grease | 10 | |
| Ammonical Nitrogen as N | 50 | |
| Total Kjeldhal Nitrogen (TKN) as N | 75 | |
| Free Ammonical Nitrogen as N | 2.0 | |
| CN concentration | 0.1 | |
| Nitrate Nitrogen as N | Urea Plant | 10 |
| Other than Urea Plant | 20 | |
| (ii) Straight Phosphatic Fertilizer Plant | ||
| pH | 6.5 to 8.5 | |
| Suspended Solids | 100 | |
| Oil and Grease | 10 | |
| Fluoride | 10 | |
| Dissolved Phosphate as P | 5.0 | |
| (iii) Complex Fertilizer Plant and / orNP/NPK(N-Nitrogen, P-Phosphorus and K-Potassium) | ||
| pH | 6.5 to 8.5 | |
| Suspended Solids | 100 | |
| Oil and Grease | 10 | |
| Ammonical Nitrogen as N | 50 | |
| Total Kjeldhal Nitrogen (TKN) as N | 75 | |
| Free Ammoniacal Nitrogen as N | 4.0 | |
| Total Kjeldhal Nitrogen (TKN) as N | 75 | |
| Free Ammoniacal Nitrogen as N | 4.0 | |
| Nitrate Nitrogen as N | 20 | |
| Dissolved Phosphate as P | 5.0 | |
| Fluoride as F- | 10 | |
| Note:(i)Chromium salt shall not be used in cooling tower as algaecide.(ii) The effluent shall be analysed for Vanadiumand Arsenic once in a year and analysis report shall be submittedto the concerned State Pollution Control Board / PollutionControl Committee. | ||
| B .- Emission Standards | ||
| (i) Straight Nitrogenous | ||
| (a) Ammonia Plant- Reformer | ||
| Oxides of Nitrogen (as NO2) | 400 mg/Nm3 | |
| (b) Urea Plant – Prilling Tower | ||
| Particulate Matter | Pre 1982 units | 150 mg/Nm3 |
| Post 1982 units | 50 mg/Nm3** | |
| (ii) Ammonium Nitrate/ Calcium AmmoniumNitrate/NPK plant | ||
| Particulate Matter | Existing Plant | 150 mg/Nm3 |
| New Plant | 100 mg/ Nm3 | |
| Ammonium as NH3 | Existing Plant | 300 mg/Nm3 |
| New Plant | 150 mg/Nm3 | |
| Total Fluoride as F- | 10 mg/Nm3(only NPK Plant) | |
| (iii) Phosphatic Fertilizer Plants –Phosphoric Acid Plants/ Rock grinding and Acidulation SSP Plants | ||
| Particulate Matter | 125 mg/Nm3 | |
| Total Fluoride as F- | 20 mg/Nm3 | |
| (iv) Nitric Acid Plant | ||
| Oxides of Nitrogen (as NO2) | 400 mg/Nm3 | |
| *Values to bereported at 3% O2** Total emission of0.5 kg/ tonne of product.Note:(i)Fluoride norms shall be applicable only for NPK plant.(ii) Plantcommissioned on or after the date of notification, shall betreated as 'New Plant'.(iii) The height ofthe stack emitting Sulphur Dioxide, Oxides of Nitrogen or Oxidesof Phosphorus or acid mist shall be a minimum of 30 metres or asper the formula H=14 (Q)0.3, whichever is more, where “H”is the height of stack in metres and “Q” is themaximum quantity of SO2 NOx or P2O5 equivalent expected to beemitted in kg/hr through the stack at 100 per cent rated capacityof the tail gas plant(s) and calculated as per the norms ofgaseous emission.(iv) Tail Gas plantshaving more than one stream or unit of Sulphuric Acid, NitricAcid or Phosphoric Acid at one location, the combined capacity ofall the streams or units for a particular acid shall be takeninto consideration for determining the stack height andapplicability of emission standards individually.(iii) Tail gas plants having separate stack forgaseous emission for the scrubbing unit, the height of this stackshall be equal to main stack or 30 metres, whichever is higher.] |
| 18. Iron OreMining and Ore Processing | A.Emission Standards for Stack for De-dusing Unit | |||
| Particulatematter | 100mg/Nm3 | |||
| Stackheight** | 15.0 m | |||
| **Stack height for De-dusting unit shall be calculated as H=74 Q0.27, where H and Q are stack height in metre and particulatematter (PM) emission in tonner/hr respectively, i.e. | ||||
| Q(kg/hr)Up to 2.712.72 – 7.867.87 –17.9617.97 – 35.29 | H(metre)15202530 | |||
| Note:-Stackattached to De-dusting unit shall have minimum height of 15.0metres and would be atleast 2.50 metres above the top-most pointof the nearby building/shed or plant in the mine. | ||||
| B.Fugitive Emission Standards | ||||
| Particulatematter | 1200µ100mg/Nm3 | |||
| Note:-Fugitive emission shall be monitored in the predominant downwinddirection at a distance0 25.0+2.0 metres from the source offugitive emission as per following : | ||||
| Area | Monitoringlocation | |||
| Mine face/Benches | Drillingexcavation and loading applicable for operation benches abovewaterable | |||
| Haul Roads/ServiceRoads | Haul roads to oreprocessing plant, waste dumps and loading areas and service road | |||
| Crushing plant | Run-off mineunloading at hopper, crushing areas, screens and transfer points. | |||
| Screening Plant | Screens, conveyingand transportation of ore discharge points | |||
| Ore Storage andLoading | Intermediate stockbin/pile areas ore stock bin/pile areas , wagon/truck loadingareas | |||
| Waste dump | Activewaste/reject dumps | |||
| C.Effluent Standards | ||||
| pH | 5.5-9.0 | |||
| Suspendedsolids (non-rainy day) | 50mg/l | |||
| Suspendedsolids (railny day) | 100mg/l | |||
| Oiland grease | 10mg/l | |||
| Note:-(I)All efforts shall be made to reuse and rel-circulate the treatedeffluent.(ii) The aforesaid effluent standards shall becomplied with for sewage, service water, beneficiation of orewashwater and surface run-off put together | ||||
| 19. CalciumCarbide | Particulate MatterEmission : | |||
| -Kiln | 250 milligrammeper normal cubic metre | |||
| -Arc Furnace | 150 milligrammeper normal cubic metre | |||
| 20. Carbon Black | Particulate MatterEmission : | 150 milligrammeper normal cubic metre | ||
| 21. [] Copper, Leador Zinc Smelting Plant | Emission standards | |||
| a. ConcentratorExisting Unit | New Unit | |||
| Particulate Matter(mg/Nm3) | 100 | 75 | ||
| b. Sulphur-DioxideRecovery Unit Limitting Concentration in mg/Nm3 Plant capacityfor 100% convertible concentration of Sulphuric Acid (time/day) | Existing Unit | New Unit | ||
| Sulphur-Dioxide(So2) | Upto300 | 1370 | 1250 | |
| Above300 | 1250 | 950 | ||
| Acid Mist/SulphurTrioxide | Upto300 | 90 | 70 | |
| Above300 | 70 | 50 | ||
| Note:-1. Capacity in above stipulation means the installedcapacity of Sulphuric Acid Plant.2. Scrubbing units shallhave on-line pH meters with auto recording facility.3. Plantcommissioned on or after the date of notification, shall betermed as 'New Unit.'4. The height of the Stack emittingSulphur Dioxide or acid mist shall be a minimum of 30 meters oras per the formula H = 14(Q)0.3(whichever is more),where “H” is the height of stack in metres; and “Q”is the maximum quantity of SO2in kg/hr, expected tobe emitted through the stack at 110 per cent rated capacity ofthe Tail Gas plant(s) and calculated as per the norms of gaseousemission.5. Tail Gas plants having more than one stream orunit of sulphuric acid at one location, the combined capacity ofall the streams or units shall be taken into consideration fordetermining the stack height and applicability of emissionstandards.6. Tail Gas plants having separate stack forgaseous emission for the scrubbing unit, the height of this stackshall be equal to main stack or 30 metres, whichever is higher. | ||||
| 22. Nitric Acid(emission oxides of nitrogen) | Emission of Oxidesof Nitrogen | 3 kilogramme ofoxides of nitrogen per tone of weak acid (before concentration)produced | ||
| 23. [ SulphuricAcid Plant] | Emission standards | |||
| Limitingconcentration in mg/Nm3, unless started | ||||
| Plant capacity for100% concentration of Sulphuric | ExistingUnit | NewUnit | ||
| Acid (tonne/day) | ||||
| Sulphur dioxide | (SO2)up to 300 | 1370 | 1250 | |
| Above 300 | 1250 | 950 | ||
| Acid Mist/Sulphur | Up to 300 | 90 | 70 | |
| Trioxide | Above 300 | 70 | 50 | |
| Note. - (i)Scrubbing units shall have on-line pH meter with auto recordingfacility. | ||||
| (ii) The height ofthe stack emitting sulphur-dioxide or acid mist shall be ofminimum of 30 metre or as per the formula H = 14 (Q)(0.3)(whichever is more). | ||||
| Where "H"is the Height of stack in metre; and "Q" is the maximumquantity of So2expected to be emitted through thestack at 110 per cent rated capacity of the plants and calculatedas per the norms of gaseous emission. | ||||
| (iii) Plantshaving more than one stream or unit of sulphuric acid at onelocation, the combined capacity of all the streams and unitsshall be taken into consideration for determining the stackheight and applicability of emission standards. | ||||
| (iv) Plants havingseparate stack for gaseous emission for the scrubbing unit, theheight of this stack shall be equal to main stack.] | ||||
| S.No. | Industry | Parameter | Standard | |
| 24. | Integrated Ironand Steel Plant | A-Coke oven(by-product type) | ||
| a. EffluentStandards | ||||
| Limitingconnecntration in mg/l, except for pH | ||||
| pH | 6.0-8.50 | |||
| Suspended solids | 100 | |||
| BOD, 3 days at27°C | 30 | |||
| COD | 250 | |||
| Oil and grease | 10 | |||
| Ammonical nitrogenas N | 50 | |||
| Cyandie (as CN-) | 0.2 | |||
| Phenol | 1.0 | |||
| b. EmissionStandards | ||||
| New Batteries (atgreen field site) | Rebuild Batteries | Existing Batteries | ||
| (i) FugitiveVisible Emission | ||||
| Leakage from door | 5(PLD)* | 10(PLD)* | 10(PLD)* | |
| Leakage fromcharging lids | 1(PLL)** | 1(PLL)** | 1(PLL)** | |
| Leakage from APCovers | 4(PLO)+ | 4(PLO)+ | 4(PLO)+ | |
| Charging emission(Second/charge) | 16(with HPLA) | 50(with HPLA) | 75 | |
| *PLD- Percentleaking doors; **PLL-Percent leaking lids; | ||||
| +PLO- PercentLeaking off takes and HPLA- Aspiration through high pressureliquor injection in gooseneck. | ||||
| (ii) (StackEmission Standards) | ||||
| SO2 (mg/Nm3) | 800 | 800 | 800 | |
| NOx (mg/Nm3) | 500 | 500 | 500 | |
| Particulate matter(mg/Nm3) | 50 | 50 | 50 | |
| Particulate matterduring charging of stamp charging batteries (mg/Nm3) | 25 | 25 | 25 | |
| Sulphur in COkeOven gas used for heating (mg/Nm3) | 800 | - | - | |
| (iii) FugitiveEmission: Benzo (a) Pyrene (BaP) | ||||
| Battery area (topof the battery)(µg/m3) | 5 | 5 | 5 | |
| Other units inCoke oven plant (µg/m3) | 2 | 2 | 2 | |
| B.-Sintering Plant | ||||
| a. EffluentStandards | ||||
| Limitingconcentration in mg/l, except of pH | ||||
| pH | 6.0-8.50 | |||
| Suspended solids | 100 | |||
| Oil and grease | 10 | |||
| b. EmissionStandards | ||||
| Particulate matter(mg/Nm3) | 150 | |||
| C.- Blast Furance | ||||
| a. EffluentStandards | ||||
| Limitingconcentration in mg/l, except for pH | ||||
| pH | 6.0-805 | |||
| Suspended solids(mg/l) | 50 | |||
| Oil and grease(mg/l) | 10 | |||
| Cyanide as CN(mg/l) | 0.2 | |||
| Ammonical Nitrogen | 50 | |||
| as NH3-N (mg/l) | ||||
| b. EmissionStandards | ||||
| (i) StackEmissions | ||||
| NewUnits | ExistingUnits | |||
| BF Stove | ||||
| Particulate matter(mg/Nm3) | 50 | 30 | ||
| SO2 (mg/Nm3) | 250 | 200 | ||
| Nox (mg/Nm3) | 150 | 150 | ||
| CO (Vol/Vol) | 1%(max) | 1%(max) | ||
| (ii) SpaceDeducting/Other Stacks of BF area | ||||
| Particulate matter(mg/Nm3) | 100 | 50 | ||
| (iii) FugitiveEmission | ||||
| ExistingUnits | NewUnits | |||
| Particulate matter(Size less than 10 microns) PM10 (µg/m3) | 4000 | 3000 | ||
| SO2 (µg/m3) | 200 | 150 | ||
| NOx (µg/m3) | 150 | 120 | ||
| Carbon monoxide(µg/m3)- 8 hours | 5000 | 5000 | ||
| 1hours | 10,000 | 10,000 | ||
| Lead, as Pb infugitive dust (µg/m3) at Cast House | 2 | 2 | ||
| D.- Steel MakingShop-Basic Oxygen Furnace | ||||
| a. EffluentStandards | ||||
| pH (mg/l) | 6.0-8.5 | |||
| Suspended solids(mg/l) | 100 | |||
| Oil and grease(mg/l) | 10 | |||
| (i) Stack Emission | ||||
| Existing Units | New Units | |||
| Converters | ||||
| Particulate matter(mg/Nm3) | ||||
| - Blowing/Lancingoperation | 300 | Should be with gasrecovery | ||
| - Normal operation | 150 | Should be with gasrecovery | ||
| **SecondaryFmission Stack : De-dusting of de-sulphurisation, Secondaryrefining etc. | ||||
| Particulate matter(mg/Nm3) | 100 | 50 | ||
| (ii) FugitiveEmission | ||||
| ExistingUnits | NewUnits | |||
| Particulate matter(size less than 10 microns) PM10 (µg/m3) | 4000 | 3000 | ||
| SO2 (µg/m3) | 200 | 150 | ||
| NOx (µg/m3)- 8 hours | 5,000 | 5,000 | ||
| 1 hours | 10,000 | 10,000 | ||
| Lead, as Pb indust at Converter floor (µg/m3) | 2 | 2 | ||
| E- Rolling Mills | ||||
| a. EffluentStandaeds | ||||
| pH | 6.0-9.0 | |||
| Suspended solids(mg/l) | 100 | |||
| Oil and grease(mg/l) | 10 | |||
| b. EmissionStandards | ||||
| Particulate matter(mg/Nm3) | 150 | |||
| Re-Heating | ||||
| Sensitivearea | Otherarea | |||
| Particulate matter(mg/Nm3) | 150 | 250 | ||
| F.- Arc Furnaces | ||||
| Emission Standards | ||||
| Particulate matter(mg/Nm3) | 150 | |||
| G.- InductionFurnaces | ||||
| Emission Standards | ||||
| Particulate matter(mg/Nm3) | 150 | |||
| H.- CupolaFoundary | ||||
| Emission Standards | ||||
| melting capacityless than 3 tonne/hr | melting capacity 3tonne/hr and above | |||
| Particulate matter(mg/Nm3) | 450 | 150 | ||
| SO2 (mg/Nm3) | 300, corrected at12% CO2 | |||
| I.- CalcinationPlant/Lime Kiln/Dolomite Kiln | ||||
| Emission Standards | ||||
| capacity upto40t/day | capacity above40t/dat | |||
| Particulate matter(mg/Nm3) | 500 | 150 | ||
| J.- RefractoryUnit | ||||
| Emission Standards | ||||
| Particulate matter(mg/Nm3) | 150 | |||
| Note :1.The height of the each process stack shall be a minimum of 30metres or as per the formula H = 14(W)0.3 (Whichever is more),where "H" is the height of stack in metre; and "Q"is the maximum quantity of SO2 in kg/hr expected to be emittedthrough the stack at rated capacity of the plant(s) andcalculated as per the norms of faseous emission.2. The Plantshaving separate stack for gaseous emission for the scrubbingunit, the height of this stack shall be equal to main stack ofthe plant or 30 metres, whichever is higher. 3. It is essentialthat stack constructed over the cupola beyond the charging doorand emissions shall be directed through the stack which should beat least six times the diameter of cupola.4. In respect ofArc Furnaces and induction Furnaces provision shall be made forcollecting the fumes before discharging the emissions through thestack.5. Foundries shall install scrubber, followed by astack of height atleast six times the diameter of the Cupolabeyond the charing door.6.Recovery type converters shall beinstalled in new plants or expansion projects. | ||||
| Note:(i)Stromwater shall not be allowed to mix with effluent, scrubberwater and/or floor washings.(ii) Stormwater shall bechannellized through separate drains as per natural gradient,passing through High Density Polyethlene (HDPE) lined pits, eachhaving holding capacity of 10 minutes (hourly average) ofrainfall. | ||||
| 25. [ Thermal PowerPlants] | Particulate MalterEmissions : | |||
| -generationcapacity 210 MW or more | 150 milligrammeper normal cubic meter | |||
| -generationcapacity less than 210 MW | 350 milligrammeper normal cubic meter |
| 26.[***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | ||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| 27. [ All types of Asbestos manufacturing units (including all processes involving the use of Asbestos)] [Inserted by G.S.R. 913(E), dated 24-10-1989 (w.e.f. 24-10-1989).] | Emissions | |
| [-Pure Asbestos material [Substituted by Notification No. G.S.R. 46(E) dated 3.2.2006 (w.e.f. 19.11.1986)] | 0.5 fibre */cc for one year from the date of notification | |
| 0.2 fibre */cc after one year from the date of notification] | ||
| -Total dust | 4 Fibre */cc | |
| 2 mg/m3(normal) | ||
| 28. Chlor Alkali (Caustic soda) | Emissions | Concentrations in mg/m3(normal) |
| (a) mercury Cell | Mercury (from hydrogen gas holder stack) | 0.2 |
| (b) All processes | Chlorine (from hypo tower) | 15.0 |
| (c) All processes | Hydrochloric acid vapours and mist(from hydrochloric acid plant) | 35.0 |
| 29. Large pulp and paper | Emissions | Concentrations in mg/m3(normal) |
| Particulale matter | 250** | |
| H2S | 10 |
| 30. Integrated Iron and Steel PIants: | Emissions | |
| (a) Coke oven | Particulate matter | 50 |
| (b) Refractory material plant | Particulate matter | 150 |
| II. Effluents | Concentration in mg/litre (except for pH) | |
| (a) Coke oven By-product plant : | pH | 6.0-8.5 |
| Suspended solids | 100 | |
| Phenol | 1.0 | |
| Cyanide | 0.2 | |
| [BOD (3 days at 27°C)] | 30 | |
| COD | 250 | |
| Ammonical nitrozen | 50 | |
| Oil Grease | 10 | |
| (b) Other plants such as sintering plant, blast furnace, steel melting and rolling mill : | pH | 6.0-9.0 |
| Suspended solids | 100 | |
| Oil Grease | 10 | |
| 31. Re-heating (Reverberatory) | Emissions | Concentrations in mg/m3(normal) |
| Furnaces: | ||
| Capacity: All sizes | 150 | |
| Sensitive area | Particulate matter | |
| Other area | Particulate matter | 450] |
| 32. [ Foundries] [Inserted by G.S.R. 742(E), dated 30-8-1990 (w.e.f. 30-8-1990).] | Emissions | |
| (a) Cupola | ||
| Capacity (Melting rate): | ||
| Less than 3 Mt/hr. | Particulate matter | 450 |
| 3 MT/hr. and above | Particulate matter | 150 |
| (b) Arc Furnaces | ||
| Capacity: All sizes | Particulate matter | 150 |
| (c) Induction Furnaces | ||
| Capacity: All sizes | Particulate matter | 150 |
| 33. Thermal PowerPlants | StackHeight /Limits | |
| Power generationcapacity: | ||
| - 500 MW andabove | 275 | |
| - 200 MW/210 MWand above to less than 500 MW | 220 | |
| - Less than 200MW /210 MW | H=14(Q)0.3where Q is emission rate of SO2in kg/hr. and H Stackheight in meters. | |
| Stream generationcapacity: | ||
| - Less than 2ton/hr. | 2-1/2 times theneighboring building height or 9 metres (whichever is more). | |
| - More than 2ton/hr. to 5 ton/hr. | 12 | |
| - More than 5ton/hr. to 10 ton/hr. | 15 | |
| - More than 10ton/hr. | 18 | |
| - More than 15ton/hr. to 20 ton/hr. | 15 | |
| - More than 20ton/hr. to 25 ton/hr. | 24 | |
| - More than 25ton/hr. to 30 ton/hr. | 27 | |
| - More than 30ton/hr. | 30 or usingformula H=14(Q)0.3(whichever is more) where Q isemission rate of SO2in kg/hr. and H is Stack heightin metres. |
| 34. Small Boilers | Emissions* | |||
| Capacity of Boiler | Particulate matter | |||
| -Iess than 2ton/hr. | 1600 | |||
| -2 to 15 ton/hr. | 1200 | |||
| -More than 15ton/hr. | 150 | |||
| *All emissionsnormalized to 12 per cent carbon dioxide. | ||||
| 35. [ CoffeeIndustry] | Instant/DryProcessing | |||
| Limiting value forconcentration in mg/1 except for pH | ||||
| pH | 6.5-8.5 | |||
| BOD3days, 27°C | 100 | |||
| Total DissolvedSolids | 2100 | |||
| Wet/ParchmentCoffee Processing | ||||
| pH | 6.5-8.5 | |||
| BOD3days, 27°C | 1000 | |||
| Notes. - | ||||
| (i) Coffee growershaving plantation area less than 10 ha with wet processing shallstore primary treated effluent in lined lagoons for solarevaporation with a non-permeable system at the base and sides oflagoon. | ||||
| (ii) Coffeegrowers having plantation are between 10-25 ha with wetprocessing shall store primary (equalisation and neutralisation)treated effluent in lined lagoons for solar evaporation with anon-permeable system at the base and sides of lagoon. | ||||
| (iii) Coffeegrowers having plantation area 25 ha or above with wet processingshall store secondary treated effluent in conformity with abovenorms in lined lagoons with a non-permeable lining system at thebase and sides of lagoon and use the effluent for irrigationafter dilution so as BOD of diluted effluent for land applicationis less than 100 mg/1. | ||||
| (iv) The minimumliner specifications for a non-permeable lining system shall be acomposite barrier having 1.5 mm High Density Polyethylene (HDPE)geomembrane or equivalent, overlying 90 cm of soil (clay oramended soil) having permeability coefficient not more than1x10-5cm/sec. | ||||
| (v) The effluentstorage facilities/lagoons/solar evaporation ponds shall belocated above high flood level mark of the nearly stream,revulet, etc., with below mentioned free board and away from anywater body/stream at a distance. | ||||
| Grower → | Small | Medium | ||
| ( 10 ha) | (10 – 25 ha) | |||
| Free Board (cm) → | 30 | 60 | ||
| Distance (m) → | 50 | 100 | ||
| (vi) Raw, Treatedand/or diluted effluent shall not be discharged into surfacewater body or used for recharging ground water under anycircumstances what | ||||
| 36. AluminiumPlants | Emissions | |||
| (a) Alumina Plant: | ||||
| (i) Raw MaterialHandling | Primary andSecondary Crusher | 150 | ||
| Particulate matter | ||||
| (ii) PrecipitationArea | Particulate Matter | 250 | ||
| -Calcinations | Carbon Monoxide | 1% max. | ||
| Stack height | H = 14 (Q)(0.3)where Q is emission rate of SO2in kg/hr. and His Stack height in metres | |||
| (b) Smelter Plant | ||||
| (i) Green AnodeShop | Particulate matter | 150 | ||
| (ii) [ Anode BakeOven [Substituted by Notification No. G.S.R. 46(E) dated 3.2.2006 (w.e.f. 19.11.1986)] | -do- | 50 mg/Nm3 | ||
| (iii) Pot room | Total Fluoride | 2.8 kg/ton by 31stDecember 2006 | ||
| For Soderberg*Technology | ||||
| For Pre-bakedTechnology | 0.8 kg/ton by 31stDecember 2006 | |||
| *Separatestandards for VSS, HSS, PBSW and PBCW as given in column 4 standsabolished.] | ||||
| (c) Standards for forage fluoride - | ||||
| -Twelveconsecutive months average | 40 ppm | |||
| -Two consecutivemonths average | 60 ppm | |||
| -One month average | 80 ppm] | |||
| *37. StoneCrushing Unit | Suspendedparticulate matter (SPM) | The Standardsconsist of two parts: | ||
| (i) Implementationof the following Pollution Control measures: | ||||
| (a) Dustcontainment cum suppression system for the equipment. | ||||
| (b) Constructionof wind breaking walls. | ||||
| (c) Constructionof the metalled roads within the premises. | ||||
| (d) Regularcleaning and wetting of the ground within the premises. | ||||
| (e) Growing of agreen belong along the periphery. | ||||
| (ii) Quantitativestandard for the SPM: | ||||
| TheSuspended Particulate Matter contribution value at a distance of40 metres from a controlled isolated as well as from a unitlocated in a cluster should be less than 600 mg/Nm3.The measurements are to be conducted at least twice a month forall the 12 months in a year. | ||||
| 38. Petrochemicals(Basic intermediates) | [A. Effluents] | |||
| PH | 6.5-8.5 | |||
| [*BOD (3days at27°C)] | 50 | |||
| **Phenol | 5 | |||
| Sulphide (as S) | 2 | |||
| COD | 250 | |||
| Cyanide ( as CN) | 0.2 | |||
| ***Fluoride (as F) | 15 | |||
| Total suspendedsolids | 1000 | |||
| Hexavalent | 0.1 | |||
| Chromium (asCR+6)] | ||||
| ****Total Chromium(as CR) | 2.0 | |||
| B.Emission from Chimney/Stack | ||||
| Limitingconcentration in mg/Nm3, unless stated | ||||
| "(Furnace,Boiler, Heater, Vaporiser) | FuelType | Existingplants | NewPlant/Expansion of Existing Plant | |
| Sulphur Dioxide(SO2) | Gas | 50 | 50 | |
| Liquid | 1700 | 850 | ||
| Oxides of Nitrogen(NOx) | Gas | 350 | 250 | |
| Liquid | 450 | 350 | ||
| Particulate Matter(PM) | Gas | 10 | 05 | |
| Liquid | 100 | 50 | ||
| Carbon Monoxide(CO) | Gas | 150 | 100 | |
| Liquid | 200 | 150 | ||
| Note,- | ||||
| (i)All values shall be corrected to 3% Oxygen.(ii)Wet scrubber shall necessarily be operated at the time ofdecoking.(iii)Norms for CO shall be monitored only in case of PhthalicAnhydride (PA), Maleic Anhydride (MA), Terephthalic Acid (PTA)and Dimethyl Terephalate (DMT) Plants. Norms for CO emissionsshall not be applicable to PA/MA manufacturing standaloneexisting piants with an installed capacity of less than 30,000metric tonnes per annum, provided that such units have achimney/stack of minimum 30 metres height for emitting CarbonMonoxide. | ||||
| ProcessEmission (Specific Pollutant) | ||||
| Source | Limitingconcentration in mg/Nm3 | |||
| ExitingPlants | NewPlants | |||
| Chlorine | EDC/VCM Plant andIncinerator | 10 | 10 | |
| Hydrochloric AcidMist | EDC/VCM Plant andIncinerator | 30 | 30 | |
| Ammonia | Wastewaterstripper, acrylonitrile plant, carpolacturm plant | 75 | 75 | |
| Hydrogen Sulphide | Naphthapre-treatment plant, olefin plant | 05 | 05 | |
| Phosgene | (TDI) and (MDI)plant | 01 | 01 | |
| HydrogenCyanide(HCN) | Acrylonitrileplant | 10 | 10 | |
| VOC (HAPs)-TDI andMDI | TDI,Methylenediphenyl Di-isocyante (MDI) Plants | 0.1 | 0.1 | |
| VOC (HAPs),Benzene and Butadiene | Benzene, ButadienePlants | 5.0 | 5.0 | |
| VOC(HAPs), EO, VCM, EDC, ACN and PO | EO, VCM, EDC, ACN,PO Plants | 20.0 | 10.0 | |
| OrganicParticulate | PA, MA and TDIPlants | 50 | 25 | |
| ProcessEmission (General Pollutant) | ||||
| Source | Limitingconcentration in mg/Nm3 | |||
| VOC (MA, PA andPhenol) | MA, PA, PhenolPlants | 20 | ||
| VOC (EB, Styrene,Toluene, Xylene, Aromatics, EG and PG) | Ethyl benzene(EB), Styrene, Toluene, Xylene, Aromatics, EG, PG Plants | 10 | ||
| VOC (Paraffin,Acetone and Olefins) | Non-methane, HC(paraffin), Acetone, Olefins Plants | 150 |
| (Emission controlfor Road tank, truck/Rail tank, wagon loading) | |||
| Loading ofVolatile Products | Naphtha:(i)VOC reduction,%or(ii) Emission, gm/m3 | (i) _99.5or(ii) _ 5 | |
| Benzene andButadience:(i) VOC reduction,%or(ii) Emission, mg/m3 | (i) _99.99or(ii) _ 20 | ||
| Toluene/Xylene:(VOC)reduction,%or(ii) Emission, mg/m3 | (i) _99.98or(ii) _ 150 |
| Sr.No. | Industry | Parameter | Standards |
| 1 | 2 | 3 | 4 |
| 39 | HotelIndustry | EffluentStandards | |
| (i) Hotel with atleast 20 bedrooms | |||
| limiting concentration in mg/1, except for pH | |||
| Inland Surface Water | On land for Irrigation | ||
| pH | 5.5-9.0 | 5.5-9.0 | |
| BOD3days, 270C | 30 | 100 | |
| Total Suspended Solids | 50 | 100 | |
| Oil Grease | 10 | 10 | |
| Phosphate as P | 1 | - | |
| (ii) Hotel with less than 20 bedrooms or aBanquet Hall with minimum floor area of 100 m2or a Restaurantwith minimum seating capacity of 36 | |||
| pH | 5.5-9.0 | 5.5-9.0 | |
| BOD3days, 270C | 100 | 100 | |
| Total Suspended Solids | 100 | 100 | |
| Oil Grease | 10 | 10 | |
| Notes:i. Hotels, banquethalls, restaurants, etc. located in coastal area shall alsocomply with the provisions of the Coastal Regulation Zone, asapplicableii. If, the effluentis discharged into a municipal sewer leading to a SewageTreatment Plant, the hotel or restaurant or banquet hall, as thecase may be, shall provide a proper Oil and Grease Trap foreffluent arising from its kitchen and laundry and shall have tocomply with the 'General Standards for Discharge of EnvironmentalPollutants Part-A: Effluents' notified under Schedule-VI |
| Prior to its omission, serial number 39 reads a under :-{| | ||
| "39. Pharmaceutical Manufacturing and Formulation Industry | Effluents | |
| 1. pH | 5.5-9.0 | |
| 2. Oil and Grease | 10 | |
| 3. Total Suspended solids | 100 | |
| 4. [BOD (3 days at 27°C)] | 30 | |
| 5. Bio-assay test | 90% survival of fish after 96 hrs. in 100% effluent | |
| 6. Mercury | 0.01 | |
| 7. Arsenic Chromium | 0.20 | |
| 8. Chromium (Hexavalent) | 0.10 | |
| 9. Lead | 0.10 | |
| 10. Cyanide | 0.10 | |
| 11. Phenolics (as C6H5OH) | 1.00 | |
| 12. Sulphides (as S) | 2.00 | |
| 13. Phosphates (as P) | 5.00 |
| S.No. | Industry | Parameter | Standard |
| (1) | (2) | (3) | (4) |
| A.Emission Standards | |||
| 40 | Pesticide Industry | Limitingconcentration in mg/Nm3 | |
| HCI | 20 | ||
| Cl2 | 5 | ||
| H2S | 5 | ||
| P2O5as H3PO4 | 10 | ||
| NH3 | 30 | ||
| Pesticidescompounds in the form of particulate matter | 20 | ||
| CH3CI | 20 | ||
| HBr | 5 | ||
| B.Effluent Standards | |||
| Limitingconcentration in mg/l, except for pH and Bioassay test | |||
| (i)Compulsory Parameters | |||
| pH | 6.5-8.5 | ||
| BOD, 3 days, 27°C | Formulation unit | 30 | |
| Technical graedunit | 100 | ||
| Oiland Grease | 10 | ||
| SuspendedSolids | 100 | ||
| BioassayTest | 90percent survival of fish after 96 hours in 100% effluent* | ||
| (ii)Additional Parameters | |||
| Arsenic(as As) | 0.2 | ||
| Copper | 1.0 | ||
| Manganese | 1.0 | ||
| Mercury | 0.01 | ||
| Antimony(as Sb) | 0.1 | ||
| Zinc | 1.0 | ||
| Nickel, etc.(heavy metals individually) | Shall not exceedindividually 5 times the drinking water standards as per Bureauof Indian Standards | ||
| Cyanide(as CN) | 0.2 | ||
| Nitrate(as NO3) | 50 | ||
| Phosphate(as P) | 5.0 | ||
| Phenoland Phenolic Compounds as C6H5OH | 1.0 | ||
| Sulphur | 0.03 | ||
| BenzeneHexachloride (BHC) | 0.01 | ||
| Carbonyl | 0.01 | ||
| CopperOxychloride | 9.6 | ||
| DDT | 0.01 | ||
| Dimethoate | 0.45 | ||
| 24D | 0.4 | ||
| Endosulfan | 0.01 | ||
| Fenitothrion | 0.01 | ||
| Malathion | 0.01 | ||
| Methylparathion | 0.01 | ||
| Paraquat | 2.3 | ||
| Phenathoate | 0.01 | ||
| Phorate | 0.01 | ||
| Proponil | 7.3 | ||
| Pyrethrums | 0.01 | ||
| Ziram | 1.0 | ||
| OtherPesticide (individually) | 0.10 | ||
| *Bioassay Testshall be carried out as per IS: (6582-1971).Note:1.The concerned State Pollution Control Board/Pollution ControlCommittee shall prescribe limits of Total Dissolved Solids (TDS),Sulphates and Chlorides depending on the usages of recipientwater body in down stream, in which effluent shall be disposedoff.2. No limit for chemical Oxygen Demand (COD) isprescribed but, COD in the treated effluent shall be monitored.If COD is persistently reported more than 250 mg/l, theindustrial units discharging such an effluent shall be requiredto identify chemical causing the same. In case, these are foundto be toxic, as defined in Schedule I of the Manufacture, Storageand Import of Hazardous Chemicals Rules, 1989, the concernedState Pollution Control Board/Pollution Control Committee in suchcases shall direct the industries to install tertiary treatmentsystem by 31st MArch, 2012.3. Parameters listed as"Additional parameters" shall be prescribed dependingupon the process and product, on a case basis. | |||
| C.Emission Standards for Incinerator | |||
| Limitingconcentration in mg/Nm3, unless stated | Sampling Durationin minutes, unless stated | ||
| ParticulateMatter | 50 | 30 or more (forsampling of 300 litres of emission) | |
| HCI | 50 | 30 | |
| SO2 | 200 | 30 | |
| CO | 100 | Dailyaverage | |
| Totalorganic Carbon | 20 | 30 | |
| Total Dioxins andFurans* | ExistingIncinerator | 0.2ng TEQ//Nm3 | 8hours |
| New Incinerator | 0.1ng TEQ/NM3 | 8hours | |
| Sb+As+Pb+Cr+Co+Cu+Mn+Ni+Vand their compounds | 1.5 | 2hours | |
| *The existingplant shall comply with norms for Dioxins and Furans as 0.1 ngTEQ/Nm3 by 18th August, 2013.Note :i. Allmonitored values shall be corrected to 11% oxygen on drybasis.ii. The CO2 concentration in tail gas shall not be lessthan 7%. iii. In case, halogenated organic waste is less than 1%by weight in input waste, all the facilities in single chamberincinerators shall be designed so as to achieve a minimumtemperature of 1100°C in the incinerator. For fluidized bedtechnology based incinerator, temperature shall be maintained at950°C.iv. In case, halogenated organic waste is less than1% by weight in input waste, waste shall be incinerated only intwin chamber incinerators and all the facilities shall bedesigned to achieve a minimum temperature of 850±25°Cin primary chamber and 1100°C in secondary combustion chamberwith a gas residence time in secondary combustion chamber notless than two seconds.v. Scrubber meant for scrubbingemissions shall not be used as quencher. vi. Incineration plantsshall be operated (combustion chambers) with such temperature,retention time and turbulence, as to achieve Total Organic Carbon(TOC) content in the incineration ash and residue less than 3%,and their loss on ignition is less than 5% of the dry weight. Incase of non-conformity, ash and residue as the case may be, shalbe re-incinerated.vii. The incinerator shall have a chimneyof atleast thirty metres height. | |||
| D.Effluent from Incinerator | |||
| Note:(i)Stormwater shall not be allowed to mix with scrubber water and/orfloor washings.(ii) Stormwater shall be channelized throughseparate drains passing through a HDPE lined pit having holdingcapacity of 10 minutes (hourly average) of rainfull. | |||
| E.Stormwater | |||
| Note:(i)Stormwater shall not be allowed to mix with scrubber water and/orfloor washings.(ii) Stormwater shall be channelized throughseparate drains passing through a HDPE lined pit having holdingcapacity of 10 minutes (hourly average) of rainfall. |
| {| | ||
| 40. Pesticide manufacturing and Formulation Industry | Effluents | |
| 1. Temperature | Shall not exceed 5°C above the receiving water temperature | |
| 2. pH | 6.5-8.5 | |
| 3. Oil Grease | 10 | |
| 4.[BOD (3 days at 27°C)] [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | 30 | |
| 5. Total suspended solids | 100 | |
| 6. Bio-assay test | 90% survival of fish after 96% hrs. in 100% effluent | |
| 7.(a) Specific Pesticides: | ||
| Benzene hexachloride | 10 | |
| Carbonyl | 10 | |
| DDT | 10 | |
| Endosulfan | 10 | |
| Diamethoate | 450 | |
| Fenitrothion | 10 | |
| Malathion | 10 | |
| PhorateMethyl | 10 | |
| Parathion | 10 | |
| Phenthoate | 10 | |
| Pyrethrums | 10 | |
| Copper Oxychloride | 9600 | |
| Copper Sulphate | 50 | |
| Ziram | 1000 | |
| Sulphur | 30 | |
| Paraquat | 2300 | |
| Proponil | 7300 | |
| Nitrogen | 780 | |
| (b) Heavy Metals: | ||
| Copper | 1.00 | |
| Manganese | 1.00 | |
| Zinc | 1.00 | |
| Mercury | 0.01 | |
| Tin | 0.10 | |
| Any other metal1ike | Shall not exceed 5 | |
| Nickel, etc. | Times the drinking water standards of BIS |
| (c) Organics | ||
| Phenol and phenolic compound as C6H5OH | 1.0 | |
| (d) Inorganics : | ||
| Arsenics(as As) | 0.2 | |
| Cyanide (as CN) | 0.2 | |
| Nitrate(as NO3) | 50.0 | |
| Phosphate(as P) | 5.0 | |
| [Emissions] [Inserted by G.S.R. 46(E), dated 3-2-2006 (w.e.f. 3-2-2006).] | Not to exceed mg/NM3 | |
| HCL | 20 | |
| Cl2 | 5 | |
| H2S | 5 | |
| P2O5(as H3PO4) | 10 | |
| NH3 | 30 | |
| Particulate matter with pesticides compounds | 20 | |
| CH3Cl | 20 | |
| HBr | 5] |
2. Bio-assay test should be carried out with available species of fish in receiving water.
3. State Boards may prescribe limits of total dissolved solids (TDS) sulphates and chlorides depending on the use of recipient water body.
4. State Board may prescibe COD limit correlated with BOD limit.
5. Pesticides are known to have metabolites and isomers. If they are found in significant concentration, standards may be prescribed for those in the list by Central or State Board.
6. Industries are required to analyse pesticides in waste-water by advanced analytical method such as GLC/HPLC.
7. All the parameters will be compulsory for formulators, for others, the 7th will be optional.
|}| 41. Tannery (after primary treatment) | Effluents | |
| Disposal: Channel/Conduit | ||
| Carrying waste-waters to Secondary treatment plants | ||
| Type of Tanneries | ||
| -Chrome tanneries/combined chrome and vegetable tanneries | ||
| pH | 6.5-9.0 | |
| SS | Not to exceed 600 | |
| Chromium concentration after treatment in the chrome waste-water stream | 45 | |
| -Vegetable tanneries | pH | 6.5-9.0 |
| SS | Not to exceed 600 |
| 42. Paint Industry (Waste-water discharge) | Effluents | |
| pH | 6.0-8.5 | |
| Suspected Solids | 100 | |
| [BOD (3 days at 27°C)] [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | 50 | |
| Phenolics as C6H5OH | 1.0 | |
| Oil Grease | 10.0 | |
| Bio-assay test | 90% survival in 96 hours | |
| Lead as Pb | 0.1 | |
| Chromium as Cr. | 0.1 | |
| Hexavalent | ||
| Total | 2.0 | |
| Copper as Cu | 2.0 | |
| Nickel as Ni | 2.0 | |
| Zinc as Zn | 5.0 | |
| Total heavy metals | 7.0 | |
| 43. Inorganic Chemical Industry(Waste-Water discharge) Part I (metal compounds of Chromium, Manganese, Nickel, Lead and Mercury) | Effluents | |
| pH | 6.0-8.5 | |
| Chromium as Cr | ||
| Hexavalent | 0.1 | |
| Total | 2.0 | |
| Manganese as Mn | 2.0 | |
| Nickel as Ni | 2.0 | |
| Copper as Cu | 2.0 | |
| Zinc as Zn | 5.0 | |
| Cadmium as Cd | 0.2 | |
| Lead as Pb | 0.1 | |
| Mercury as Hg | 0.01 | |
| Cyanide as CN | 0.2 | |
| Oil Grease | 10.0 | |
| Suspended solids | 30.0 | |
| Note. - In addition to the above, total heavy metals are to be limited to 7mg/l. | ||
| 44. Bullion Refining (Waste-water discharge) | Effluents | |
| pH | 6.5-8.5 | |
| Cyanide as CN | 0.2 | |
| Sulphide as S | 0.2 | |
| Nitrate as N | 10.0 | |
| FreeCl2as Cl | 1.0 | |
| Zinc as Zn | 5.0 | |
| Copper as Cu | 2.0 | |
| Nickel as Ni | 2.0 | |
| Arsenic as As | 0.1 | |
| Cadmium as Cd | 0.2 | |
| Oil and Grease | 10.0 | |
| Suspended Solids | 100 | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | ||
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | |
| [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] | [* * *] [Omitted by Notification No. G.S.R. 485 (E) dated 9.6.2010 (w.e.f. 19.11.1986)] |
| Sl. No. | Category | Standards, Db (A) |
| 1 | 2 | 3 |
| 46. | Noise Limits for Automobiles (Free Field at one meter in dB(A) at the Manufacturing Stage) to be Achieved by the Year 1992. | |
| (a) Motorcycle, Scooters Three Wheelers | 80 | |
| (b) Passenger Cars | 82 | |
| (c) Passenger or Commercial Vehicles upto 4 MT | 85 | |
| (d) Passenger or Commercial Vehicles above 4 MT and upto 12 MT | 89 | |
| (e) Passenger or Commercial Vehicles exceeding 12 MT | 91 | |
| 47. | Domestic Appliances and Construction Equipments at the manufacturing Stage to be achieved by the Year, 1993 | |
| (a) Window Air Conditioners of 1 ton to 1.5 ton | 68 | |
| (b) Air Coolers | 60 | |
| (c) Refrigerators | 46 | |
| [***] [Item (d) omitted by G.S.R. 371(E), dated 17-5-2002 (w.e.f. 17-5-2002).] | ||
| (e) Compactors (rollers) Front loaders, Concrete mixers, Cranes (movable), Vibrators and Saws. | 75] |
| Sl. No. | Industry | Parameter | Standards |
| 1 | 2 | 3 | 4 |
| 48. [] [Inserted by G.S.R. 93(E), dated 21-2-1991 (w.e.f. 27-2-1991)] | GlassIndustry | Emissions | |
| A. | SodalimeBorosilicate and other special Glass (other than Lead) | ||
| (a) Furnace: | |||
| Capacity | |||
| (i) Upto aproduct draw capacity of 60 MT/Day | Particulatematter | 2.0 kg/hr. | |
| (ii) Productdraw capacity more than 60 MT/Day | Particulatematter | 0.8 kg./Mt.of product drawn | |
| (iii) For allcapacities emission and H is stack height in metres. | Stack height | H=14(Q)0.3where Q is the rate of SO2in Kg/hr. | |
| Totalfluorides | 5.0 mg/NM3 | ||
| NOX | Use of lownox burners in new plants. | ||
| (b)Implementation of the following measures for fugitive emissioncontrol from other sections :- | |||
| (i) Rawmaterials should be transported in leak proof containers. | |||
| (ii) Culletpreparation should be dust-free using water spraying. | |||
| (iii) Batchpreparation section should be covered. | |||
| B. | Lead Glass | ||
| (a) Furnace: | |||
| Allcapacities | Particulatematter | 50 mg/NM3 | |
| Lead | 20 mg/NM3 | ||
| (b)Implementation of the following measures for fugitive emissioncontrol from other sections :- | |||
| (i) Batchmixing, proportioning section and transfer points should becovered and it should be connected to control equipments to meetthe following standards: | |||
| Particulatematter | 50 mg/NM3 | ||
| Lead | 20 mg/NM3 | ||
| (ii) MinimumStack height should be 30 metres in lead glass units. | |||
| (c) PotFurnace at Firozabad | |||
| Furnace : | Particulatematter | 1200 mg/NM3 | |
| Note :-Depending upon local' environmental conditions, State/ CentralPollution Control Board can Particulate matter prescribe morestringent standards than those prescribed above. | |||
| C. | GlassIndustry (For all categories) | Effluents | |
| pH | 6.5-8.5 | ||
| TotalSuspended solids | 100 mg/l | ||
| OilGrease | 10 mg/l | ||
| 49 | Lime Kiln | Stack height | |
| Capacity:- | Stack height | ||
| Upto 5T/day | A Hood shouldbe provided with a stack of 30 meter height from ground level(including kiln height). | ||
| Above 5T/day | Stack height | H=14 (Q)0.3Where Q is emission rate of SO2in kg/hr. and H isStack Height in meters. | |
| More than5T/day | Particulatematter | 500 mg/NM3 | |
| And upto40T/day | |||
| Above 40T/day | Particulatematter | 150 mg/NM3 | |
| [50 [Substituted by Notification No. G.S.R. 1016(E), dated 28.10.2016 (w.e.f. 19.11.1986).] | A.Slaughterhouses or Meat ProcessingUnits or Both* | Effluents | MaximumConcentration values are in mg/l exceptfor pH |
| pH | 6.5 to 8.5 | ||
| Bio-chemicalOxygen Demand(BOD) [3 daysat 27°C] | 30 | ||
| ChemicalOxygen Demand(COD) | 250 | ||
| SuspendedSolids | 50 | ||
| Oil andGrease | 10 | ||
| B.Sea FoodIndustry* | Bio-chemicalOxygen Demand(BOD) [3 daysat 27°C] | 30 | |
| SuspendedSolids | 50 | ||
| Oil andGrease | 10 | ||
| *Theemission standards from Boiler House of Slaughterhouses or MeatProcessing Units or both and Sea Food Industry shall conform tothe standards prescribed vide notification No. G.S.R. 742 (E),dated 30.08.1990 as amended from time to time under theEnvironment (Protection) Act, 1986.Note:(i)For Slaughterhouses operating in local bodies/ municipalities,where the treated effluent is discharged into municipal sewersleading to full-fledged Sewage Treatment Plant, the BOD may berelaxed to 100mg/l.(ii)All Slaughterhouses/ meat processing units shall ensure safe andproper disposal of solid waste {Type I (Vegetable matter such asrumen, stomach and intestinal contents, dung, agricultureresidues etc) and Type II (Animal matter such as inedible offal,tissues, meat trimmings, waste and condemned meat, bones etc.)}through suitable technology approved by SPCBs/ PCCs.] |
| Sl. No. | Industry | Parameter | Standards | |
| 1 | 2 | 3 | 4 | |
| 51. | *Food and Fruit Processing Industry: | Effluents | Concentration not to exceed mg/1except pH | Quantum gm/MT of product |
| Category : | ||||
| A. | Soft Drinks | |||
| (a) Fruit based/Synthetic(More than 0.4 MT/Day) bottles and tetra pack | ||||
| pH | 6.5-8.5 | - | ||
| Suspended solids | 100 | |||
| Oil and grease | 10 | |||
| [BOD (3 days at 27°C)] [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | 30 | |||
| (b) Synthetic (Less than 0.4 MT/Day) | Disposal via septic tank | - | ||
| B. | FruitVegetables | |||
| (a) Above 0.4 MT/Day | pH | 6.5-8.5 | - | |
| Suspended solids | 50 | |||
| Oil and grease | 10 | |||
| [BOD (3 days at 27°C)] | 30 | |||
| (b) 0.1-0.4 MT/Day | Disposal via septic tank | - | ||
| (10 MT/Yr) | ||||
| C. | Bakery | |||
| (a) Bread and Biscuit | ||||
| (i) Continuous process | ||||
| (more than 20T/Day) | pH | 6.5-8.5 | ||
| [BOD (3 days at 27°C)] | 200 | 25 | ||
| (ii) Non-continuous process (less than 20MT/Day) | Disposal via septic tank | |||
| (b) Biscuit Production | ||||
| (i)10 T/Day above | pH | 6.5-8.5 | ||
| [BOD (3 days at 27°C)] [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | 300 | 35 | ||
| (ii) Below 10T/Day | Disposal via septic tank | |||
| D. | Confectioneries | Effluents | ||
| (a) 4 T/Day and above | pH | 6.5-8.5 | ||
| Suspended solids | 50 | |||
| Oil and grease | 10 | |||
| [BOD (3 days at 27°C)] | 30 | |||
| (b) Below 4 T/Day | Disposal via septic tank |
| Sl. No. | Industry | Parameter | Standards |
| 1 | 2 | 3 | 4 |
| 52. | *Jute Processing Industry: | Effluents | Concentration in mg/1except pH and water consumption. |
| pH | 5.5-9.0 | ||
| [BOD (3 days at 27°C)] | 30 | ||
| Suspended solids | 100 | ||
| Oil and grease | 10 | ||
| Water consumption | 1.60 Cum/Ton of product produced. |
2. At the present no limit for colour is given for liquid effluent. However, as far as possible colour should be removed.
*Stack emissions from boiler house shall conform to the standards already prescribed under Environment (Protection) Act, 1986 vide Notification-No. GSR 742(E), dated 30th August, 1990.| 53. Large Pulp Paper/News Print/Rayon Grade Plants of[Capacity above 24,000 MT per annum] [Substituted by G.S.R. 546(E), dated 30-8-2005 (w.e.f. 30-8-2005).] | Effluents | Concentration in mg/1except pH and TOCL |
| pH | 7.0-8.5 | |
| [BOD (3 days at 27°C)] | 30 | |
| COD | 350 | |
| Suspended solids | 50 | |
| [Absorbable Organic Halogens (AOX) in effluent discharge [Substituted by G.S.R. 546(E), dated 30-8-2005 (w.e.f. 30-8-2005).] | 1.5kg/ton of product with effect from the date of publication of this notification 1.0 kg/ton of product with effect from the 1stday of March, 2008] | |
| Flow (Total waste-water discharge) | ||
| **(i) Large pulp and paper | 200 Cum/Ton of paper produced | |
| (ii) Large rayon grade/News Print | 150 Cum/Ton of paper produced |
| 54. Small Pulp and Paper, Paper Plant of Capacity upto 24,000 MT/Annum: | Effluents | |
| Category : | ||
| A.* Agro-based | Total Waste-water discharge | 200 Cum/Ton of paper produced |
| B. **Waste-paper based | -do- | 75 Cum/Ton of paper produced |
| 55. Common Effluent Treatment Plants: | Effluents | ||||
| A. Primary Treatment | (Inlet effluent quality for CETP) | (Concentration in mg/1) | |||
| pH | 5.5-9.0 | ||||
| Temperature °C | 45 | ||||
| Oil Grease | 20 | ||||
| Phenolic Compounds (as C6H5OH) | 5.0 | ||||
| Ammonical Nitrogen (as N) | 50 | ||||
| Cyanide (as CN) | 20 | ||||
| Chromium hexavalent (as Cr+6) | 2.0 | ||||
| Chromium (total) (as Cr) | 2.0 | ||||
| Copper (as Cu) | 3.0 | ||||
| Lead (as Pb) | 1.0 | ||||
| Nickel (as Ni) | 3.0 | ||||
| Zinc (as Zn) | 15 | ||||
| Arsenic (as As) | 0.2 | ||||
| Mercury (as Hg) | 0.01 | ||||
| Cadmium (as Cd) | 1.0 | ||||
| Selenium (as Se) | 0.05 | ||||
| Fluoride (as F) | 15 | ||||
| Boron (as B) | 2.0 | ||||
| Radioactive Materials | |||||
| Alpha emitters, ục/ml | 10-7 | ||||
| Beta emitters, ục/ml | 10-8 | ||||
| Note.- 1. These standards apply to the small scale industries, i.e., total discharge upto 25 KL/Day. | |||||
| 2. For each CETP and its constituent units, the State Board will prescribe standards as the local needs and conditions; these can be more stringent than those prescribed above. However, in case of clusters of units, the State Boards with the concurrence of CPCB in writing may prescribe suitable limits. | |||||
| Into inland surface waters | On land for Irrigation | Into Marine Coastal areas | |||
| (a) | (b) | (c) | |||
| B. Treated Effluent Quality of common effluent treatment plant | Concentration in mg/l except pH and Temperature | ||||
| pH | 5.5-9.0 | 5.5-9.0 | 5.5-9.0 | ||
| [BOD (3 days at 27°C)] | 30 | 100 | 100 | ||
| Oil Grease | 10 | 10 | [10] [Substituted for the words "20" by Notification No. G.S.R. 739 (E) dated 9.9.2010 (w.e.f. 19.11.1986)] | ||
| Temperature | Shall not exceed 40°C in any Section of the stream within 15 metres downstream from the effluent outlet. | 45°C at the point of discharge | |||
| Suspended solids | 100 | 200 | (a) For process waste-waters 100 | ||
| (b) For cooling water effluents 10 per cent. above totalsuspended matter of in effluent cooling water | |||||
| Dissolved Solids (Inorganic) | 2100 | 2100 | - | ||
| Total residual chlorine | 1.0 | - | 1.0 | ||
| Ammonical nitrogen (as N) | 50 | - | 50 | ||
| Total Kjeldahl Nitrogen (as N) | 100 | - | 100 | ||
| Chemical Oxygen Demand | 250 | - | 250 | ||
| Arsenic (as As) | 0.2 | 0.2 | 0.2 | ||
| Mercury (as Hg) | 0.01 | - | 0.01 | ||
| Lead (as Pb) | 0.1 | - | 1.0 | ||
| Cadmium (as Cd) | 1.0 | - | 2.0 | ||
| Total Chromium (as Cr) | 2.0 | - | 2.0 | ||
| Copper (as Cu) | 3.0 | - | 3.0 | ||
| Zinc (as Zn) | 5.0 | - | 15 | ||
| Selenium (as Se) | 0.05 | - | 0.05 | ||
| Nickel (as Ni) | 3.0 | - | 5.0 | ||
| Boron (as B) | 2.0 | 2.0 | - | ||
| Percent Sodium | - | 60 | - | ||
| Cyanide (as CN) | 0.2 | 0.2 | 0.2 | ||
| Chloride (as CI) | 1000 | 600 | - | ||
| Fluoride (as F) | 2.0 | - | 15 | ||
| Sulphate (as S04) | 1000 | 1000 | - | ||
| Sulphide (as S) | 2.8 | - | 5.0 | ||
| Pesticides | Absent | Absent | Absent | ||
| Phenolic compounds C6H5OH | 1.0 | - | 5.0 | ||
| Note.- All efforts should be made to remove colour and unpleasant odour as far as possible.] | |||||
| 56. Dairy | Effluents | Concentration in mg/1, except pH | Quantum per product processed | ||
| pH | 6.5-8.5 | - | |||
| *[BOD (3 days at 27°C)] | 100 | - | |||
| **Suspended Solids | 150 | - | |||
| Oil and Grease | 10 | - | |||
| Waste-water generation | - | 3m3/kl of milk | |||
| Note.- *BOD may be made stringent upto 30 mg/l if the recipient fresh water body is a source for drinking water supply. BOD shall be upto 350 mg/l for the chilling plant effluent for applying on land provided the land is designed and operated as a secondary treatment system with suitable monitoring facilities. The drainage water from the land after secondary treatment has to satisfy a limit of 30 mg/l of BOD and 10 mg/l of nitrate expressed as "N". The net addition to the groundwater quality should not be more than 3 mg/l of BOD and 3 mg/l of nitrate expressed as "N". This limit for applying on land is allowed subject to the availability of adequate land for discharge under the control of the industry, BOD value is relaxable upto 350 mg/l, provided the waste-water is discharged into a town sewer leading to secondary treatment of the sewage. | |||||
| ** Suspended solids limit is relaxable upto 450 mg/l, provided the waste-water is discharged into town sewer leading to secondary treatment of the sewage. | |||||
| 57. Tanneries Effluents | Effluents | Concentration in mg/1, except pH | Quantum per raw hide processed | ||
| pH | 6.5-9.0 | ||||
| [BOD (3 days at 27°C)] | 100 | ||||
| Suspended Solids | 100 | - | |||
| Sulphides (as S) | 1 | - | |||
| Total Chromium (as Cr) | 2 | - | |||
| Oil and Grease | 10 | - | |||
| Waste-water generation | - | 28m3/T | |||
| *For effluent discharge into inland surface waters BOD limit shall be made stricter to 30 mg/l by the concerned State Pollution Control Board. | |||||
| 58.[***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | ||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | ||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | ||||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |||||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |||||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |||||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |||||
| [***] [Deleted by Notification No. G.S.R. 221 (E) dated 18.3.2011 ] | |||||
| 59. [ Agriculture residue fired Boilers (including bagasse)] [Substituted by Notification No. G.S.R. 647 (E) dated 13.9.2002 (w.e.f. 19.11.1986)] | Emissions | (Concentration in mg/1) | |||
| (a) Step grate | Particulate matter | 250 | |||
| (b) Horse shoe/pulsating grate | Particulate matter | 500(12% CO2) | |||
| (c) Spreader stroker | Particulate matter | 800(12% CO2) | |||
| Note.- In the case of horse shoe and spreader stroker boilers, if more than one boiler is attached to a single stack, the Standard shall be fixcd based on added capacity of all the boilers connected with the stack. | |||||
| 60. Man-made fibre industry(Semi-Synthetic). | Effluent | Concentration in mg/1 except for pH | |||
| pH | 5.5-9.0 | ||||
| Suspended Solids | 100 | ||||
| [BOD (3 days at 27°C)] | 30 | ||||
| Zinc (as Zn) | 1 | ||||
| 61. Ceramic Industry | Emissions | (Concentration in mg/Nm3) | |||
| A. Kilns | |||||
| (a) Tunnel, Top Hat, Chamber | Particulate matter | 150 | |||
| Flouride | 10 | ||||
| Chloride | 100 | ||||
| Sulphurdioxide | ** | ||||
| (b) Down-draft | Particulate matter | 1200 | |||
| Fluoride | 10 | ||||
| Chloride | 100 | ||||
| Sulphurdioxide | ** | ||||
| (c) Shuttle | Particulate matter | 250 | |||
| Flouride | 10 | ||||
| Chloride | 100 | ||||
| Sulphurdioxide | ** | ||||
| (d) Vertical shaft Kiln | Particulate matter | 250 | |||
| Flouride | 10 | ||||
| Sulphurdioxide | ** | ||||
| (e) Tank furnace | Particulate matter | 150 | |||
| Flouride | 10 | ||||
| Sulphurdioxide | ** | ||||
| B. Raw Material handling, Processing and operations | |||||
| (a) Dry raw material handling and processing operations | Particulate matter | 150 | |||
| (b) Basic raw materials and processing operations | Particulate matter | * | |||
| (c) Other sources of air pollution generation | Particulate matter | * | |||
| C. Automatic spray unit | |||||
| (a) Drayers | |||||
| (i) Fuel fired dryers | Particulate matter | 150 | |||
| (ii) For heat recovery dryers | Particulate matter | * | |||
| (b) Mechanical finishing operation | Particulate matter | * | |||
| (c) Lime/plaster ofParismanufacture | Particulate matter | * | |||
| Capacity | Stack height | ||||
| Upto 5T/day | -do- | A. Hood should be provided with a stack of 30 metre height from ground level (including kiln height) | |||
| Above 5T/day | -do- | H=14(Q)0.3Where Q is emission rate of SO2in/kg/hr and H is Stack height in metres | |||
| More than 5T/day and upto 40T/day | Particulate matter | 500 mg/Nm3 | |||
| -do- | 150 mg/Nm3 |
| Coal Consumed per day | Stack Height |
| Less than 8.5 mt. | 9 m. |
| More than 8.5 to 21 mt. | 12 m. |
| More than 21 to 42 mt. | 15 m. |
| More than 42 to 64 mt. | 18 m. |
| More than 64 to 104 mt. | 21 m. |
| More than 104 to 105 mt. | 24 m. |
| More than 105 to 126 mt. | 27 m. |
| More than 126 mt. | 30 m. or using formula H-14 (Qg)0.3(whichever is more) |
| 62. [ Viscose Filament Yarn (Sub-sector of man-made fibre semi-Synthetic Industry)] [Added by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | Effluents | (Concentration In mg/l except for pH) |
| pH | 5.5-9.0 | |
| Suspended solids | 100 | |
| [BOD(3 days at 27°C)] [Substituted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | 30 | |
| Zinc (as Zn) | 5 | |
| 63. [ Starch Industry (Maize products)] [Inserted by G.S.R. 176(E), dated 2-4-1996 (w.e.f. 3-4-1996).] | Effluents | Concentration not to exceed mg/l (except pH and waste-water discharge) |
| pH | 6.5-8.5 | |
| BOD | 100 | |
| (3 days at 27°C) | ||
| Suspended solids | 150 | |
| Waste-water discharge | 8 m3/tonne of maize processed |
| 64. Beehive hard coke oven | Emission: | 150 mg/Nm3 |
| (i) New unit | Particulate matter (corrected to 6%CO2) | |
| Hydrocarbons | 25 ppm | |
| (ii) Existing units | Particulate matter (corrected to 6%CO2) | 350 mg/Nm3 |
| 65. Briquette Industry (Coal) | Emission: | |
| (a) Units having capacity less than 10tonnes. | Particulate matter (corrected to 6%CO2) | 350 mg/Nm3 |
| (b) Units having capacity 10 tonnes or more. | Particulate matter (corrected to 6%CO2) | 150 mg/Nm3 |
| 66.Soft Coke Industry | Particulate matter (corrected to 6% CO2) | 350mg/Nm3 |
| 67. Edible Oil Vanaspati Industry | Effluents | |
| Temperature | Not more than 5°C above ambient temperature of the recipient water body. | |
| pH | 6.5-8.5 | |
| Suspended solids | 150 mg/l | |
| Oil and grease | 20 mg/l | |
| BOD(3 days at 27°C) | 100 mg/l | |
| COD | 200 mg/l | |
| Waste-water discharge | ||
| (i) Solvent extraction | 2.0 cum/tonne of product (oil) | |
| (ii) Refinery/Vanaspati(refined oil Vanaspati) | 2.0 cum/tonne of product | |
| (iii) Integrated unit of solvent extraction and refinery/vanaspati | 4.0 cum/tonne of refined oil/vanaspati produced | |
| (iv) Barometric cooling water/De-odoriser water | 15.0 cum/tonne of refined oil/vanaspati |
| Sl.No. | Industry | Parameter | Standard | |
| (1) | (2) | (3) | (4) | |
| 68. | Organic Chemicals Manufacturing Industry | A. Effluent Standards | ||
| Limiting concentration in mg/1, except for pH and Bioassaytest | ||||
| Compulsory parameters | ||||
| pH | 6.5-8.5 | |||
| BOD 3 days, 27°C | 100 | |||
| Oil Grease | 10 | |||
| Bioassay test + | Minimum 90% survival after 96 hours in 100%effluent Additional parameters | |||
| Nitrate (as N) | 10 | |||
| Arsenic (as As) | 0.2 | |||
| Chromium Total | 1.0 | |||
| Lead (as pb) | 0.1 | |||
| Cyanide (as CN) | 0.2 | |||
| Zinc (as Zn) | 5.0 | |||
| Mercury (as Hg) | 0.01 | |||
| Copper (as Hg) | 2.0 | |||
| Nickel (as Nil) | 2.0 | |||
| Phenolics (as C6 H5 OH) | 5.0 | |||
| Sulphide | 2.0 | |||
| + The Bioassay test shall be conducted as per IS: 6582+-1971 | ||||
| Note:(i) Industries covered underthis group include halo aliphatics, plasticizers, aromatics(alcohols, phenols, esters, acids and salts, aldehydes andketones), substituted aromatics, aliphatics (alcohols, esters,acids, aldehydes, ketones amines and amides) and detergents.(ii)Though norms for COD are not mentioned here but, COD shall bemonitored. If the COD in treated effluent exceeds 250 mg/1, theconcerned industrial units discharging such effluent shall berequired to identify chemicals responsible for high COD ineffluent shall be required to identify chemicals responsible forhigh COD in effluent. In case, these are found to be toxic asdefined under the Manufacture, Storage and Import of HazardousChemicals Rules, 1989, the concerned industry shall installtertiary treatment system.(iii) The above mentioned standardsshall not be applicable to small scale detergent formulatingunits. | ||||
| B. Emission Standards for Incinerator | ||||
| Limiting concentration in mg/Nm3, unless otherwise stated | Sampling Duration in minutes unless otherwisestated | |||
| Particulate Matter | 50 | 30 or more (for sampling about 300 litres ofemission) | ||
| HCI | 50 | 30 | ||
| SO2 | 200 | 30 | ||
| CO | 100 | daily average | ||
| Total Organic Carbon | 20 | 30 | ||
| Total Dioxins Existing and Furans* Incinerator- | 0.2 ng TEQ/Nm3 | 8 hours | ||
| New Incinerator | 0.1 ng TEQ/Nm3 | 8 hours | ||
| Sb+As+Pb+Cr+Co+Cu+Mn+Ni+V+Cd+Th+Hg and their compounds | 1.5 | 2 hours | ||
| *The existing plant shall comply with norms forDioxins and Furans as 0.1 ng TEQ/Nm3 by 1st January, 2014. | ||||
| Note:(i) All monitored values shallbe corrected to 11% oxygen on dry basis.(ii) The CO2concentration in tail gas shall not be less than 7%.(iii) Incase, halogenated organic waste is less than 1% by weight ininput waste all the facilities in twin chamber incinerator shallbe designated so as to achieve a minimum temperature of 850±25°in primary chamber and 950°C in secondary combustion chamberand with a gas residence time in secondary combustion chamber notless than twoorall the facilities in single chamberincinerator for gaseous hazardous waste shall be designated so asto achieve a minimum temperature of 950° in the combustionchamber with a gas residence time not less than two seconds.(iv)In case halogenated organic waste is more than 1% by weight ininput waste, waste shall be incinerated only in twin chamberincinerators and all the facilities shall be designated toachieve a minimum temperature of 850±25° C in primarychamber and 1100°C in secondary combustion chamber with a gasresidence time in secondary combustion chamber not less than twoseconds.(v) Scrubber meant for scrubbing emissions shall notbe used as quencher.(vi) incineration plants shall beoperated (i.e. combustion chambers) with such temperature,retention time and turbulence, as to achieve Total Organic Carbon(TOC) content in the incineration ash and residue less than 3%and their loss on ignition is less than 5% of them weight. Incase of non-conformity, ash and residue, as the case may be shallbe re-incinerated.(vii) The incinerator shall have a chimneyof at least thirty meters height. | ||||
| C. Effluent Standards for Incinerator | ||||
| Note:(i) Effluent from scrubber (s)and floor washing shall flow through claosed conduit or pipenetwork and be treated to comply with the effluent standardsmention at 'A' above(ii) The built up in Total DissolvedSolids Solids (TDS) in waste water of floor washings shall notexceed 1000 mg/over and above the TDS of raw water used. | ||||
| D. Storm water | ||||
| Note:(i) Storm water shall not be allowed to mixwith scrubber water and/or floor washings.(ii) Storm watershall be channellized through separate drains passing through aHDPE lined pit having holding capacity of 10 minutes (hourlyaverage) of rainfall. |
| {| | ||
| 68. Organic Chemicals manufacturing industry | Effluents | |
| (a) Compulsory parameters | ||
| pH | 6.5-8.5 | |
| BOD(3 days at 27°C) | 100mg/l | |
| Oil and grease | 10mg/l | |
| Bio-assay test | Minimum 90%survival after 96 hours with fish at 100% effluent) | |
| (b) Additional parameters | (mg/1) | |
| Nitrate (as N) | 10 | |
| Arsenic | 0.2 | |
| HexavalentChromium | 0.1 | |
| Total Chromium | 1.0 | |
| Lead | 0.1 | |
| Cyanide as CN | 0.2 | |
| Zinc | 0.5 | |
| Mercury | 0.01 | |
| Copper | 2.0 | |
| Nickel | 2.0 | |
| Phenolicsas C6H5OH | 5.0 | |
| Sulphide | 2.0 |
| Sl.No. | Industry | Parameter | Standards |
| (1) | (2) | (3) | (4) |
| 69. | GrainProcessing, Flour Mills, Paddy Processing, Pulse Making orGrinding Mills | A-EmissionStandards | |
| Capacity(tonne per hour) | LimitingConcentration in mg/Nm3 | ||
| 1 to3 | 150 | ||
| Particular matter | Morethan 3 | 100 | |
| Notes:-(i)All dust generating equipments or processes shall be providedwith dust extraction arrangement.(ii) The bag houses, etc.,shall be connected to chimneys/stacks of 12 metres height or atleast 02 metres above the top most point of the building or shedor plant in the industry.(iii) The unit shall channellse shopfloor/fugitive emissions through a stack of 12 metres height orat least 02 metres above the top most point of the building orshed or plant in the industry. | |||
| B-EffluentStandards | |||
| Limitingvalue for concentration in mg/l except for pH | |||
| Inlandsurface water | Publicsewar | Landfor irrigation | |
| pH | 5.5-9.0 | 5.5-9.0 | 5.5-9.0 |
| Suspended Solids | 100 | 600 | 200 |
| Oils and Grease | 10 | 20 | 10 |
| BOD 3 days at 27°C | 30 | 350 | 100 |
| COD | 250 | - | - |
| C-StormwaterStandards | |||
| (I) Stormwater fora unit (having plot size atleast 250 square meters) shall not beallowed to mix with scrubber water, effluent and/or floorwashings.(ii) Stormwater within the battery limits of a unitshall be channelized through separate drain/pipe passing througha HDPE lined pit having holding capacity of 10 minutes (hourlyaverage) of rainfall. |
| 70. Boilers(Small) | Steam generation capacity (ton/hour) | Particulate Emission matter |
| mg/NM3 | ||
| less than 2 | 1200* | |
| 2 to less than 10 | 800* | |
| 10 to less than 15 | 600* | |
| 15 and above | 150** |
| 71. Pesticides industry | (i)Compulsory Parameters | mg/l except pH |
| pH | 6.5-8.5 | |
| BOD (3 days at 27oC) | 100 | |
| Oil Grease | 10 | |
| Suspended solids | 100 | |
| Bio-assay test | Minimum 90%survival of fish after 96 hours with 90% effluent and 10% dilution water. Test shall be carried out as per IS : 6502-1971. | |
| (ii) Additional Parameters | mg/l | |
| (a) Heavy metal | ||
| Copper | 1.0 | |
| Manganese | 1.0 | |
| Zinc | 1.0 | |
| Mercury | 0.01 | |
| Tin | 0.1 | |
| Any other like Nickel | shallnot exceed 5 times the drinking water standards (BIS) individually. | |
| (b) Organics | ||
| Phenol Phenolic Compounds as C6H5OH | 1.0 | |
| (c) Inorganics | ||
| Arsenic as AS | 0.2 | |
| Cyanide as CN | 0.2 | |
| Nitrate as NO3 | 50 | |
| Phospateas P | 5.0 | |
| (d) Specific pesticide | (microgram/litre) | |
| Benzene | 10 | |
| Hexachloride | ||
| DDT | 10 | |
| Dimethoate | 450 | |
| Copper oxychloride | 9600 | |
| Ziram | 1000 | |
| 2,4D | 400 | |
| Paraquat | 23000 | |
| Propanil | 7300 | |
| Nitrogen | 780 | |
| Other/below mentioned Pesticides individually | 100 | |
| Other pesticides : | ||
| (i)Insecticides : | ||
| AluminiumPhosphide | Lindane | Pyrethrum extract |
| Dichlorovos | Malathion | Quinalphos |
| EDTC Mixer | Methyl Bromide | Monocrotophos |
| Ethylene Dibromide | Nicotine Sulphate | Carbaryl |
| Ethion | OxydemetonMethyl | Endosulfan |
| Fenitrothion | Methyl Parathion | Fenvalerate |
| Lime-sulphur | Phosphamidon | Phorate |
| Temephos | ||
| (ii) Fungicides: | ||
| Aureofungin | Organomercurials(MEMC PMA) | |
| Barium Polysulphide | Sulphur(Colloidal, Wettable Dust) | |
| Cuprous Oxide | Steptocycline | |
| Ferbam | Thiram | |
| Mancozeb | Zineb | |
| Manab | Carbendazim | |
| Nickel Chloride | Tridemorph | |
| (iii) Rodenticides | ||
| Comafuryl | ||
| Warfarin | ||
| Zinc Phosphide | ||
| (iv) Nematicides: | ||
| MethamN-Sodium | ||
| (v)Weedicides: | ||
| Fluchloralin | ||
| Isoproturon | ||
| Butachlor | ||
| Anilphos | ||
| (vi) Plant Growth Regulants: | ||
| ChloromequatChloride | ||
| NemphaleneAcetic Acid | ||
| (vii) Any other pesticide not specified above. |
| 72. Oil Drilling and Gas Extraction Industry | ||
| A.Standards for Liquid Effluent | ||
| 1.0On-Shore facilities (For Marine Disposal) | ||
| pH | 5.5-9.0 | |
| Oil Grease | 10 mg/l | |
| Suspended solids | 100 mg/l | |
| BOD(3 days at 27°C) | 30 mg/l |
| Parameter | Toxicity limit, mg/l |
| Chromium as Cr | 0.1 |
| Copper, as Cu | 0.05 |
| Cyanide, as CN | 0.005 |
| Fluoride, as F | 1.5 |
| Lead, as Pb | 0.05 |
| Mercury, as Hg | 0.01 |
| Nickel, as Ni | 0.1 |
| Zinc, as Zn | 0.1 |
| Sl. No. | Parameter | On-shore discharge standards (Not to exceed) |
| 1 | 2 | 3 |
| 1. | pH | 5.5-9.0 |
| 2. | Temperature | 40°C |
| 3. | Suspended Solids | 100 mg/l |
| 4. | Zinc | 2 mg/l |
| 5. | BOD | 30 mg/l |
| 6. | COD | 100mg/1 |
| 7. | Chlorides | 600 mg/l |
| 8. | Sulphates | 1000 mg/l |
| 9. | TDS | 2100 mg/l |
| 10. | %Sodium | 60 mg/l |
| 11. | Oil and Grease | 10 mg/l |
| 12. | Phenolics | 1.2 mg/l |
| 13. | Cyanides | 0.2 mg/l |
| 14. | Fluorides | 1.5 mg/l |
| 15. | Sulphides | 2.0 mg/l |
| 16. | Chromium (Cr+6) | 0.1 mg/l |
| 17. | Chromium (Total) | 1.0 mg/l |
| 18. | Copper | 0.2 mg/l |
| 19. | Lead | 0.1 mg/l |
| 20. | Mercury | 0.01 mg/l |
| 21. | Nickel | 3.0 mg/l |
1. Disposal of Drill Cuttings and Drilling Fluids for On-shore Installations:
2. Disposal of Drill Cutting and Drilling Fluids for Off-shore Installations:
| 73. [ Pharmaceutical (Manufacturing and Formulation) Industry] [Substituted by G.S.R. 512(E), dated 9-7-2009 (w.e.f. 9-7-2009).] | Effluent Standards | |
| (i)Compulsory Parameters | Limiting concentration in mg/1, expect for pH | |
| pH | 6.0-8.5 | |
| Oil grease | 10 | |
| BOD (3 days 27°C) | 100* | |
| Total suspended solids | 100 | |
| Bioassay Test | 90% survival of fish after first 96hours in 100% effluent** | |
| (ii) Additional Parameters | ||
| Mercury | 0.01 | |
| Arsenic | 0.20 | |
| Chromium (Cr6+) | 0.10 | |
| Lead | 0.10 | |
| Cyanide | 0.10 | |
| Phenolics(C6H5SOH) | 1.0 | |
| Sulphides(as S) | 2.0 | |
| Phosphate (as P) | 5.0 |
| [A. Emission from Incinerator] | ||||
| Limiting concentration in mg/Nm3, Unless stated | Sampling duration in (minutes) unless stated | |||
| Particulate Matter | 50 | 30 or more (for sampling about 300 litre emission) | ||
| HCI | 50 | 30 | ||
| SO2 | 200 | 30 | ||
| CO | 100 | 30 | ||
| Total Organic Carbon | 20 | 30 | ||
| Total Dioxins and Furans* | Existing Incinerator | 0.2 ng TEQ/Nm3 | 8 hours | |
| New Incinerator | 0.1 ng TEQ/Nm3 | 8 hours | ||
| Sb+As+Pb+Cr+Co+Cu+Mn+Ni+V+Cd+Th+Hgand their compounds | 1.5 | 2 hours | ||
| *The existing plant shall comply with norms for dioxins andfurans as 0.1 ng/TEQ/ Nm3within 5 years from the dateof notification. | ||||
| Notes. - (i) All monitored values shall be corrected to 11%oxygen on dry basis. | ||||
| (ii) The CO2concentration In tall gas shall not beless than 7%. | ||||
| (iii) In case, halogenated organic waste is less than 1% byweight in input waste, all the facilities in twin chamberincinerator shall be designed so as to achieve a minimumtemperature of 850 ± 25°C in primary chamber and 950°Cin secondary combustion chamber and with a gas residence time insecondary combustion chamber not less than 2 (two) seconds. | ||||
| or | ||||
| all the facilities in single chamber incinerator for gaseoushazardous waste shall be designed so as to achieve a minimumtemperature of 950°C in the combustion chamber with a gasresidence time not less than 2 (two) seconds. | ||||
| (iv) In case halogenated organic waste is more than 1% byweight in input waste, waste shall be incinerated only in twinchamber incinerators and all the facilities shall be designed toachieve a minimum temperature of 850 ± 25°C in primarychamber and 1100°C in secondary combustion chamber with a gasresidence time in secondary combustion chamber hot less than 2(two seconds). | ||||
| (v) Scrubber meant for scrubbing emissions shall not be usedas quencher. | ||||
| (vi) Incineration plants shall be operated (combustionchambers) with such temperature, retention time and turbulence,as to achieve Total Organic Carbon (TOC) content in theincineration ash and residue less than 3%, and their loss onignition is less than 5% of the dry weight. In case ofnon-conformity, ash and/or residue shall be re-incinerated. | ||||
| (vii) The incinerator shall have a chimney of at least thirtymetre height. | ||||
| B. Effluent from Incinerator | ||||
| (i) Effluent from scrubber (s) and floor washing shall flowthrough closed conduit/pipe network. | ||||
| (ii) Storm water shall not be allowed to mix with scrubberwater and/or floor washings. | ||||
| (iii) Storm water shall be channelized through separate drainspassing through a HDPE lined pit having holding capacity of 10minutes (hourly average) of rainfall. | ||||
| (iv) The built up in Total Dissolved Solids (TDS) inwastewater of floor washings shall not exceed 1000 mg/I over andabove the TDS of raw water used. | ||||
| (v) Effluent shall not be stored in holding tank(s) in suchmanner which may cause pollution to groundwater." | ||||
| (vi) Effluent (scrubber water and floor washings) shall bedischarged into receiving water conforming to the normsprescribed under Schedule VI: General Standards for Discharge ofEnvironment Pollutions (Part A: Effluents) notified under theEnvironment (Protection) Rules, 1986. | ||||
| 74. [ Brick Kilns] [Substituted by Notification No. G.S.R. 543 (E) dated 22.7.2009 (w.e.f. 19.11.1986)] | Emission Standards | |||
| (i) Bull's Trench Kiln (BTK) | ||||
| Category* | Limiting concentration in mg/Nm3 | |||
| Particular matter | small | 1000 | ||
| medium | 750 | |||
| large | 750 | |||
| Minimum (metre) | ||||
| Stack height | small | 22 or induced draft fan operating with minimum draft of 50 mmWG with 12 metre stack height. | ||
| medium | 27 or induced draft fan operating with minimum draft of 50 mmWG with 15 metre stack height. | |||
| large | 30 or induced draft fan operating with minimum draft of 50 mmWG with 17 metre stack height. | |||
| *Category | Trench width (m) | Production (bricks/day) | ||
| small BTK | 4.50 | Less than 15,000 | ||
| medium BTK | 4.50-6.75 | 15,000-30,000 | ||
| large BTK | above 6.75 | above 30,000 | ||
| (ii) Down-Draft Kiln (DDK) | ||||
| Category++ | Limiting concentration in mg/ Nm3 | |||
| Particular matter | small/large/medium | 1200 | ||
| Minimum (metre) | ||||
| Stack height | small | 12 | ||
| medium | 15 | |||
| large | 18 | |||
| Category++ | Production (bricks/day) | |||
| Small DDK | less than 15,000 | |||
| medium DDK | 15,000-30,000 | |||
| large DDK | above 30,000 | |||
| (iii) Vertical Shaft Kiln (VSK) | ||||
| Category** | Limiting concentration in mg/ Nm3 | |||
| Particular matter | small/large/medium | 250 | ||
| Minimum (metre) | ||||
| Stack height | small | 11 (at least 5.5 m from loading platform) | ||
| medium | 14 (at least 7.5 m from loading platform) | |||
| large | 16 (at least 8.5 m from loading platform) | |||
| **Category | No. of shaft | Production (bricks/day) | ||
| small VSK | 1-3 | Less than 15,000 | ||
| medium BTK | 4-6 | 15,000-30,000 | ||
| large BTK | 7 or more | above 30,000 |
2. One chimney per shaft in Vertical Shaft Kiln shall be provided. The two chimneys emanating from a shaft shall either be joined (at the loading platform in case of brick chimney or at appropriate level in case of metal chimney) to form a single chimney.
3. The above standards shall be applicable for different kilns if coal, firewood and/or agricultural residues are used as fuel.
| Sl.No. | Industry | Parameter | Standard | |||
| (1) | (2) | (3) | (4) | |||
| [75] [Substituted by Notification No. G.S.R. 424 (E) dated 1.6.2011 (w.e.f. 19.11.1986)] | Soda Ash Industry | EffluentstandardsA. Solvay Proces | ||||
| LimitingConcentrationing mg/1 except for pH, Temperature and Bio-assay | ||||||
| Creek | Marine CoastalZone | Estuary Area | Inland SurfaceWater | |||
| Suspended Solids | 500* | 1000* | 200 | 100 | ||
| Ammonical Nitrogenas N | 50 | 50 | 50 | 50 | ||
| Oil and Grease | 5 | 5 | 5 | 5 | ||
| Bio-assay*** | Minimum 90%survival of fish after 96 hours in 100% effluent | |||||
| pH | 6.5-9.0 | |||||
| Tempertaure | Not ot exceed 5°Cabove the ambient temperature of the reveiving water body | |||||
| *The effluentdischarge point in creek shall be beyond low tide line. | ||||||
| **The diffusersystem shall be located in conformity with the Coastal RegulationZone Notification , 2011 at a minimum depth of 5 metres below lowtide level and with exit velocity for effluent more than 3metres/sec | ||||||
| ***The Bio-assaytest shall be conducted as per IS :6582-1971 | ||||||
| B.Dual Process | ||||||
| InlandSurface Water | ||||||
| ph | 6.5-9.0 | |||||
| AmmonicalNitrogen, as N | 50 | |||||
| Nitrate Nitrogen,as N | 10 | |||||
| Cyanide, as CN | 2 | |||||
| HexavalentChromium | 0.1 | |||||
| Total Chromium | 2 | |||||
| Suspended Solids | 100 | |||||
| Oil and Grease | 10 | |||||
| C.Stormwater | ||||||
| Note :- | ||||||
| (i) Stormwatershall not be allowed to mix with effluent and/or floor washings. | ||||||
| (ii) Stormwaterwithin battery limit of industry shall be channelized throughseparate drain (s) passing through HDPE lined pit(s) each havingholding capacity of 10 minutes (hourly average) of rainfall forits catchment area |
76. Emission Standard for SO² from Cupola furnace:
Standard for Sulphur Dioxide emission from Cupola Furnace :| Characteristics | Emission limit |
| Sulphurdioxide (S02) emission | 300 mg/Nm3at 12% CO2corrections |
77. Specifications of Motor Gasoline for Emission Parameters:
| Sl. No. | Characteristics | Requirement | Method of test ref. to P: of IS: 1448 |
| (i). | Reid Vapour Pressure at 38°C, Kpa | 35 to 70 | P : 39 |
| (ii). | Benzeno, Percent by volume, Max | 5.0(1) | P: 104 |
| (iii). | Lead Content(as Pb)g/l, Max | 0.15(low leaded)(2) 0.013 unleaded) | P: 38 |
| (iv). | Sulphur, percent by mass, Max | 0.10 (unleaded) 0.20 (leaded) | P : 34 |
| (v). | Potential Gum, g/m3, Max | 50 | ASTM 873 : 8 |
| (vi). | Gum (Solvent Washed)g/m3Max | 40 | P : 29 |
| (vii). | Oxygenates Content Ether (MTBE, ETBE)Alcohol,percent by volume, Max | 15 | |
| (viii). | Phosphorus | See Foot Note(3) | ASTMD 3231 |
78. Specification of Diesel Fuel for Emission Related Parameters :
| Sl. No. | Characteristics | Requirement | Method of Test Ref. to P : or IS : 1448 |
| (i) | Density at 15°C, Kg/m3 | 820 to 880 (1) | P : 32 |
| (ii) | CetaneNumber, Min | 45°0(2) | P : 9 |
| (iii) | Distillation 85 percent by volume recovery | 350 | P : 18 |
| at °C Max 95 per cent by volume recovery at °C Max | 370 | ||
| (iv) | Sulphur, percent by mass | 0.50(3) | P : 33 |
| Sl. No. | Industry | Parameter | Standards | ||
| New Batteries (at Green Field Site) | Rebuild Batteries | Existing Batteries | |||
| 79. [] [Substituted by G.S.R. 46(E), dated 3-2-2006 (w.e.f. 3-2-2006).] | Coke oven plants (by product recovery type) | Fugitive Visible Emissions | |||
| (a) Leakage from door | 5 (PLD)* | 10 (PLD)* | 10 (PLD)* | ||
| (b) Leakage from charging lids | 1 (PLL)* | 1 (PLL)* | 1 (PLL)* | ||
| (c) Leakage from AP Covers | 4 (PLO)* | 4 (PLO)* | 4 (PLO)* | ||
| (d) Charging emission (second/charge) | 16 (with HPLA)* | 50 (with HPLA)* | 75 | ||
| Stack Emission of Coke Oven | |||||
| (a) SO2(mg/Nm3) | 800 | 800 | 800 | ||
| (b) Nox(mg/Nm3) | 500 | 500 | 500 | ||
| (c) SPM (mg/Nm3) | 50 | 50 | 50 | ||
| (d) SPM emission during-charging-for stamp charging batteries (stack emission (mg/Nm3) | 25 | 25 | 25 | ||
| (e) SPM emission during coke pushing (stack emission) gm/ton of coke | 5 | 5 (applicable to stationary land based system) | - | ||
| (f) Sulphur in Coke Oven gas used for heating (mg/Nm3) | 800 | - | - | ||
| Emission for quenching operation | |||||
| (a)Batteryarea (top of the battery) | 5 | 5 | 5 | ||
| (b) Other units in coke oven plant | 2 | 2 | 2 | ||
| (c) Ambient air standards (mg/Nm3) | 10 | 10 | 10 |
| *HPLA | Aspiration through high pressure liquor injection in goose neck. |
| *PLD | Percent leaking doors; |
| *PLL | Percent leaking lids; and |
| *PLO | Percent leaking off takes. |
80. [ SPECIFICATIONS OF TWO-STROKE ENGINE OIL: [Inserted by G.S.R. 504(E), dated 20.8.1998 (w.e.f. 21.8.1998).]
| Specification | Standard | Test Procedure |
| Two-stroke engine oil grade JASO-FC as per | Minimum smoke Index of 85 | JASO-M 342-92 for JASO-FC and ASTM D-4857 for APITC |
| JASO M-345-93specification and APITC as per specification No. ASTM D 4859 |
81. [Battery manufacturing industry
| Source | Pollutant | Standards Concentration based (mg/Nm3) |
| Grid casting | Lead | 10 |
| Particulate matter | 25 | |
| Oxide manufacturing | Lead | 10 |
| Particulate matter | 25 | |
| Paste mixing | Lead | 10 |
| Particulate matter | 25 | |
| Assembling | Lead | 10 |
| Particulate matter | 25 | |
| PVC Section | Particulate matter | 150 |
| Pollutants | Concentration based standards |
| pH | 6.5-8.5 |
| Suspended solids | 50 mg/1 |
| Lead | 0.1 mg/l |
| Pollutant | Standards Concentration-based (mg/Nm3) |
| Particulate matter | 50 |
| Manganese as Mn | 5 |
| Pollutant | Concentration Based standards |
| pH | 6.5-8.5 |
| Total suspended solids | 100mg/l |
| Manganese as Mn | 2mg/l |
| Mercury as Hg | 0.02mg/l |
| Zinc as Zn | 5 mg/l |
| Pollutant | Concentration Based standards |
| Lead as Pb | 10 mg/Nmp3 |
| Particulate matter | 50 mg/Nm3 |
| Minimum stack height | 30m |
82. Environmental Standards for Gas/Naptha-based Thermal Power Plants
| Total generation of gas turbine | Limit for Stack NOx emission [v/v), at 15% excess oxygen] |
| (a)400 MW and above | (i) 50 ppm for the units burning natural gas |
| (ii) 100 ppm for the units burning naphtha. | |
| (b) Less than 400MW but Upto 100 MW | (i) 75 ppm for the units burning natural gas. |
| (ii) 100 ppm for the units burning naphtha | |
| (c) Less than 100 MW | 100 ppm for units burning natural gas or naphtha as fuel |
| (d) For the plants burning gas in a conventional boiler. | 100 ppm |
| Parameter | Maximum limit of concentration (mg/1 except for pH and temperature) |
| 2 | 3 |
| pH | 6.5-8.5 |
| Temperature | As applicable for other thermal power plants. |
| Free available chlorine | 0.5 |
| Suspended Solids | 100.0 |
| Oil and grease | 20.0 |
| Copper (total) | 1.0 |
| Iron (total) | 1.0 |
| Zinc | 1.0 |
| Chromium (Total) | 0.2 |
| Phosphate | 5.0 |
84. Temperature limit for discharge of condenser cooling Water From Thermal Power Plant :-
A: New thermal power plants commissioned after June 1, 1999:New thermal power plants, which will be using water from rivers/lakes/reservoirs shall install cooling towers-irrespective location and capacity. For thermal power plants which will use sea water for cooling purposes, the condition below will apply.B: New projects in coastal areas using sea water:The thermal power plants using sea water should adopt suitable system to reduce water temperature at the final discharge point so that the resultant rise in the temperature of receiving water does not exceed 7°C over and above the ambient temperature of the receiving water bodies.C: Existing thermal power plants:Rise in temperature of condenser cooling water from inlet to the outlet of condenser shall not be more than 10°C.D: Guidelines for discharge point:85. Environmental Standards for Coal Washeries :-
1. Fugitive emission standards.
-The difference in the value of suspended particulate matter, delta (Δ), measured between 25 and 30 metre from the enclosure of coal-crushing plant in the downward and leeward wind direction shall not exceed 150 microgram per cubic meter. Method of measurement shall be High Volume Sampling and Average Flow Rate, not less than 1.1 m³ per minute, using upwind downwind method of measurement:2. Effluent discharge standards:
-The coal washeries shall maintain the close-circuit operation with zero effluent discharge.-If in case due to some genuine problems like periodical cleaning of the system, heavy rainfall, etc., it becomes necessary to discharge the effluent to sewer/land/stream then the effluent shall conform to the following standards at the final outlet of the coal washery :| Sl. No | Parameter | Limits |
| 1. | pH | 5.5-9.0 |
| 2. | Total suspended solids | 100 mg/l |
| 3. | Oil Grease | 10 mg/l |
| 4. | B.O.D ( 3 days 27deg C) | 30 mg/l |
| 5. | COD | 250 mg/l |
| 6. | Phenolics | 1.0 mg/l |
3. Noise level standards :
-Operational/Working zone-not to exceed 85 dB(A) Leq for 8 hours' exposure.-The ambient air quality standards, in respect of noise as notified under the Environmental (Protection) Rules, 1986, shall be followed at the boundary line of the coal washery.4. Code of practice for Coal Washery:
-Water or Water mixed chemical shall be sprayed at all strategic coal transfer points such as conveyors, loading/unloading points, etc. As far as practically possible conveyors, transfer points, etc., shall be provided with enclosures.-The crushers/pulverisers of the coal washeries shall be provided with enclosures, fitted with suitable air pollution control measures and finally emitted through a stack of minimum height of 30m, conforming particulate matter emission standard of 150 mg/Nm or provided with adequate water sprinkling arrangement.-Water sprinkling by using fine atomizer nozze1e arrangement shall be provided on the coal heaps and on around the crushers/pulverisers.-Area, in and around the coal washery shall be pucca either asphalted or concreted.-Water consumption in the coal washery shall not exceed 1.5 cubic meter per tonne of coal.-The efficiency of the setting ponds of the waste-water treatment system of the coal washery shall not be less than 90 per cent.-Green belt shall be developed along the roadside,coal- handling plants, residential complex, office building and all around the boundary line of tne coal washery.-Storage bunkers, hoppers, rubber decks in chutes and centrifugal chutes shall be provided with proper rubber linings.-Vehicles movement in the coal washery area shall be regulated effectively to avoid traffic congestion. High- pressure horn shall be prohibited. Smokes emission from heavy duty vehicles operating in the coal washeries should conform the standards prescribed under Motor Vehicle Rules, 1989.86. Water quality standards for coastal waters marine outfalls.
In a coastal segment marine water is subjected to several types of uses. Depending on the types of uses and activities, water quality criteria have been specified to determine its suitability for a particular purpose. Among the various types of uses there is one use that demands highest level of water quality/purity and that is termed a "designated best use" in that stretch of the coastal segment. Based on this, primary water quality criteria have been specified for following five designated best uses :-| Class | Designated best use |
| SW-1(See Table 1.1.) | Salt pans, Shell fishing, Mariculture and ecologically Sensitive Zone. |
| SW-II (See Table 1.2) | Bathing, Contact Water Sports and Commercial fishing. |
| SW-III (See Table 1.3) | Industrial cooling, Recreation (non-contact)and Aesthetics |
| SW-IV (See Table 1.4) | Harbour |
| SW-V (See Table 1.5) | Navigation and Controlled Waste Disposal. |
| S.No. | Parameter | Standards | Rationale/Remarks |
| 1 | 2 | 3 | 4 |
| 1. | pH range | 6.5-8.5 | General broad range, Conductive for propagation of acquatic lives is given. Value largely dependant upon soil-water interaction. |
| 2. | Dissolved Oxygen | 5.0 mg/1 or 60 per cent saturation value whichever is higher | Not less than 3.5mg/1 at any time of the year for protection of acquatic lives. |
| 3. | Colourand Odour | No noticeable colour or offensive odour. | Specially caused by chemical compound like creosols, phenols, naphtha pyridine benzene, toluene, etc., causing visible colouration of salt crystal and tainting fish flesh. |
| 4. | Floating Matters | Nothing obnoxious or detrimental for use purpose. | Surfactants should not exceed an upper limit of 1.0 mg/1 and the concentration not to cause any visible foam. |
| 5. | Suspended Solids | None from sewage or industrial waste origin | Settleableinert matters not in such concentration that would impair any usages specially assigned to this class. |
| 6. | Oil and Grease(including Petroleum Products) | 0.1 mg/1 | Concentration should not exceed 0.1 mg/1 as because it has effect on fish eggs and larvae. |
| 7. [] [Substituted by G.S.R. 682(E), dated 5.10.1999 (w.e.f. 5.10.1999).] | Heavy Metals: | Values depend on : | |
| Mercury (as Hg) | 0.001 mg/1 | (i) Concentration in salt, fish and shell fish. | |
| Cadmium (as Cd) | 0.001 mg/l | (ii) Average per capita consumption per day. | |
| Lead (as Pb) | 0.01 mg/1 | (iii) Minimum ingestion rate that induces symptoms of resulting diseases. |
| S.No. | Parameter | Standards | Rationale/Remarks |
| 1 | 2 | 3 | 4 |
| 1. | pH range | 6.5-8.5 | Range does not cause skin or eye irritation and is also conducive forpropagatingaquaticlives. |
| 2. | Dissolved Oxygen | 4.0 mg/1 or 50 percent saturation value whichever is higher. | Not less than 3.5mg/1 at any time for protection of aquatic lives. |
| 3. | Colourand Odour | No noticeable colour or offensive odour. | Specially caused by chemical compound like creosols, phenols, naptha, benzene, pyridine, toluene, etc., causing visible, colouration of water and tainting of and odour in fish flesh. |
| 4. | Floating Matters | Nothing obnoxious or detrimental for use purpose | None in concentration that would impair usages specially assigned to this class. |
| 5. | Turbidity | 30 NTU (Nephelo Turbidity Unit). | Measured at 0.9m depth. |
| 6. | Fecal Coliform | 100/100 ml(MPN) | The average value not exceeding 200/100 ml. in 20 per cent of samples in the year and in 3consecutive samples in monsoon months. |
| 7. | Biochemical Oxygen Demand (BOD) (3days at 27°C) | 3 mg/1 | Restricted for bathing (aesthetic quality ofwater). Also prescribed by IS : 2296-1974. |
| S.No. | Parameter | Standards | Rationale/Remarks |
| 1 | 2 | 3 | 4 |
| 1. | pH range | 6.5-8.5 | The range is conductive for propagation of aquatic species and restoring natural system. |
| 2. | Dissolved Oxygen | 3.0 mg/1 or 40 per cent saturation value whichever is higher | To protect aquatic lives |
| 3. | Colourand Odour | No noticeable colour or offensive odour assigned to this class. | None in such concentration that would impair usages specifically assigned to this class. |
| 4. | Floating Matters | No visible, obnoxious floating debris, oil slick, scum. | As in (3) above |
| 5. | Fecal Coliform | 500/100 ml(MPN) | Not exceeding 1000/100 ml in 20 percent of samples in the year and in 3 consecutive samples in monsoon months. |
| 6. | Turbidity | 30 NTU | Reasonably clear water for Recreation, aesthetic appreciation and Industrial Cooling purposes. |
| *7. | Dissolved Iron (as Fe) | 0.5 mg/1 or less | It is desirable to have the collective concentration dissolved Fe and Mn less or equal to 0.5 mg/1 to avoid scaling effect. |
| *8. | Dissolved Manganese(as Mn) | 0.5 mg/1 or less |
| S.No. | Parameter | Standards | Rationale/Remarks |
| 1 | 2 | 3 | 4 |
| 1. | pH range | 6.0-9.0 | To minimize corrosive and scaling effect. |
| 2. | Dissolved Oxygen | 3.0 mg/1 or 40 per cent saturation value whichever is higher | Considering bio degradation of oil and inhibition to oxygen production - through photosynthesis. |
| 3. | Colourand Odour | No visible colour or offensive odour. | None from reactive chemicals which may corrode paints/ metallic surfaces |
| 4. | Floating materials, Oil, grease and scum (including Petroleum products) | 10 mg/1 | Floating matter'Should be free from excessive living organisms which may clog or coat operative parts of marine vessels/equipment. |
| 5. | Fecal Coliform | 500/100 ml(MPN) | Not exceeding 1000/100 ml in 20 per cent of samples in the year and in 3 consecutive samples in monsoon months. |
| 6. | Biochemical Oxygen Demand (3 days at 27ºC) | 5mg/1 | To maintain water relatively free from pollution caused by sewage and other decomposable wastes. |
| S.No. | Parameter | Standards | Rationale/Remarks |
| 1 | 2 | 3 | 4 |
| 1. | pH range | 6.0-9.0 | As specified by New England Inter-state Water Pollution Control Commission. |
| 2. | Dissolved Oxygen | 3.0 mg/1 or 40 percent saturation value whichever is higher | To protect aquatic lives |
| 3. | Colourand Odour | None in such concentrations that would impair any usages specially assigned to this class. | As in (i)above |
| 4. | Sludge deposits, Solid refuse floating solids oil grease and scum | None except for such small amount that may result from discharge of appropriately treated sewage and or industrial wastes effluents. | As in (1) above |
| 5. | Fecal Coliform | 500/100 ml (MPN) | Not exceeding 1000/100ml in 20 per cent of samples in the year and in 3 consecutive samples in monsoon months |
87. Emission Regulations for Rayon Industry:-
| Stack Height (H) requirement, m | Remarks |
| 11Q 0.41-3 Vs D/u | A minimum of 80 per cent. of total emission shall pass through stack. If the calculated stack height is less than 30m, a minimum height of 30m shall be provided. |
| Where | Q -CS2emission rate, kg/hr |
| VS - stack exit velocity, m/sec. | |
| D - diameter of stack, m. | |
| U - annual average wind speed at top of stack, m/sec. |
1. If there are more than one stack existing in the plant, the required height of all stacks shall be based on the maximum emission rate in any of the stacks. In other words, all the stacks carrying CS2 emission shall be of same heights (based on the maximum emission rate).
2. Number of stacks shall not be increased from the existing number. However, the number of stacks may be reduced. The existing stacks may be rebuilt and if stacks are to be relocated, condition 3 below applies.
3. Spacing among the stacks (x) at the minimum shall be 3.0 H (in m). If distance, x, between two stacks is less than 3.0 H (in m), emission shall be considered as single point source and height of both the stacks shall be calculated considering all emission is going through one stack.
88. [ Generator Sets Run on Petrol and Kerosene
A. Emission Standards- The emission standards for Generator sets on Petrol and Kerosene shall be as follows:-| Class | Displacement(CC) | CO(g/kw-hr) | HC+NOx(G/kw-hr) |
| 1 | Upto99 | _250 | _12 |
| 2 | 99and upto 225 | _250 | _10 |
| 3 | 225 | _250 | _8 |
| NoiseLimits | |
| SoundPower Level Lwa | 86dBA |
1. Applicability.- The stipulations in respect of emissions and noise referred to in entry A and entry B shall apply to all new generator sets using petrol and kerosene as fuel, manufactured in or, imported into India:
Provided that this provision shall not apply to,-2. Requirement of certification. - Every manufacturer or importer (hereinafter referred to as manufacturer) of genset (hereinafter referred to as product) to which these conditions apply shall have a separate valid certificate of type approval for all the producproduct models for emission as well as noise norms being manufactured or imported.
3. Verification of conformity of production. - Every manufacturer shall submit its products to the verification for conformity of production for emission and noise, by any of the institutions, as applicable, every conformity of production year.
4. Sale of generator sets not complying with these conditions. - The sale of product model, not having valid type approval certificate, or not complying with the emission or noise norms, as determined by the verification for conformity of production, shall continue to be prohibited in India.
5. Requirement of conformance labeling. - (1) The manufacturer of the product shall affix a conformance label on the product containing the following requirements, namely:-
(i)the label shall be durable and legible;(ii)the label shall be affixed on a part necessary for normal operation of the product and not normally requiring replacement during the product life.6. Nodal agency. - (1) The Central Pollution Control Board shall be the nodal agency for implementation of these stipulations.
7. Compliance and testing procedure. - (1) The compliance and testing procedure as published from time to time, if reviewed by Central Pollution Control Board shall be followed.
89. [ Noise standards for fire-crackers. - [Inserted by Notification No. G.S.R. 682(E), dated 5.8.1999 (w.e.f. 19.11.1986)]
A. (i) The manufacture, sale or of fire-crackers generating noise level exceeding 125 dB(AI) of 145 dB(C) at 4 metres distance from the point of bursting shall be prohibited.90. [ Standards for coal mines] [Inserted by G.S.R. 742(E), dated 25.9.2000 (w.e.f. 25.9.2000).]
1. Air Quality Standards. - The Suspended Particulate Matter (SPM), Respirable Particulate Matter (RPM), Sulphur Dioxide (SO2) and Oxides of Nitrogen (NOx) concentration in downwind direction considering predominant wind direction, at a distance of 500 metres from the following dust generating source shall not exceed the standards specified in the Tables I, II and III given below.
Dust Generating Sources. - Loading or unlading, Haul road, coal transportation road, Coal Handling Plant (CHP), Railway sliding, Blasting, Drilling, Overburden dumps, or any other dust generating external sources like coke ovens (hard as well as soft), briquette industry, nearby road, etc.TABLE I| Category | Pollutant | Time weighted average | Concentration in Ambient Air | Method of Measurement |
| 1 | 2 | 3 | 4 | 5 |
| I | Suspended Particulate Matter(SPM) | Annual Average* | 360 µg/m3 | - High Volume Sampling (Average flow rate notless than 1.1 m3/minute) |
| New Coal Mines (Coal Mines commenced operation after the date ofpublication of thisnotification) | 20 hours** | 500 µg/m3 | ||
| RespirableParticulate Matter (size less than 10 µm) (RPM) | Annual Average* | 180 µg/ m3 | RespirableParticulate Matter sampling and analysis | |
| 24 hours* | 250 µg/m3 | |||
| SulphurDioxide (SO2) | Annual Average* | 80 µg/m3 | 1. Improved west and Gaeke method | |
| 24 hours** | 120 µg/m3 | 2. Ultraviolet fluorescene | ||
| Oxide of Nitrogen as NO2 | Annual Average* | 80 µg/m3 | 1. Jacob and Hochheiser Modified (Na-Arsenic) Method | |
| 24 hours** | 120 µg/m3 | 2. Gas phase Chemiluminescence |
| Category | Pollutant | Time weighted average | Concentration in Ambient Air | Method of Measurement |
| 1 | 2 | 3 | 4 | 5 |
| II | Suspended Particulate Matter (SPM) | Annual Average* | 430 µg/m3 | - High Volume Sampling (Average flow rate not less than 1.1 m3/minute) |
| Existing coal fields/mines given below:Karanpura, Ramgarh, Giridih, Rajhara, Wardha, Nagpur Silewara, Pench Kanhan, Patharkhera, Umrer, Korba, Chirimiri, Central India Coalfields (including Baikunthpur, Bisrampur), Singrauli, lb Valley, Talcher, Godavari-Valley and any other | 24 hours** | 600 µg/m3 | ||
| RespirableParticulate Matter (size less than 10 µm) (RPM) | Annual Average* | 215 µg/ m3 | RespirableParticulate Matter sampling and analysis | |
| 24 hours* | 300 µg/m3 | |||
| SulphurDioxide (SO2) | Annual Average* | 80* µg/m3 | 1. Improved west and Gaeke method | |
| 24 hours** | 120 µg/m3 | 2. Ultraviolet fluorescene | ||
| Oxide of Nitrogen as NO2 | Annual Average* | 80 µg/m3 | 1. Jacob and Hochheiser Modified (Na-Arsenic) Method | |
| 24 hours** | 120 µg/m3 | 2. Gas phase Chemiluminescence |
| Category | Pollutant | Time weighted average | Concentration in Ambient Air | Method of Measurement |
| 1 | 2 | 3 | 4 | 5 |
| III | Suspended Particulate Matter (SPM) | Annual Average* | 500 µg/m3 | - High Volume Sampling (Average flow rate not less than 1.1 m3/minute) |
| Coal mines located in the coal fields of -- Jharia-Raniganj-Bokaro | 24 hours** | 700 µg/m3 | ||
| RespirableParticulate Matter (size less than 10 µm) (RPM) | Annual Average* | 250 µg/ m3 | RespirableParticulate Matter sampling and analysis | |
| 24 hours* | 300 µg/m3 | |||
| SulphurDioxide (SO2) | Annual Average* | 80 µg/m3 | 1. Improved west and Gaeke method | |
| 24 hours** | 120 µg/m3 | 2. Ultraviolet fluorescene | ||
| Oxide of Nitrogen as NO2 | Annual Average* | 80 µg/m3 | 1. Jacob and Hochheiser Modified (Na-Arsenic) Method | |
| 24 hours** | 120 µg/m3 | 2. Gas phase Chemiluminescence |
2. Frequency of Sampling
-Air quality monitoring at a frequency of once in a fortnight at the dust generating sources given in clause 1 shall be carried out.-As a result of monthly monitoring, if it is found that the value of the pollutant is less than 50% of the specified standards for three consecutive months, then the sampling frequency may be shifted to two days in a quarter year (3 months).-In case, the value has exceeded the specified standards, the air quality sampling shall be done twice a week. If the results of four consecutive weeks indicate that the concentration of pollutants is within the specified standards, then fortnight monitoring may be reverted to.3. Effluent Standards. - The standards for effluent discharge into sewer or stream or land, are given below :
| pH | - | 5.5-9.0 |
| Chemical Oxygen Demand (COD) | - | 250 mg/1 |
| Total Suspended Solids (TSS) | - | 100 mg/1 |
| 200 mg/1 (Land for irrigation) | ||
| OilGrease(OG) | - | 10mg/1 |
| (Monitoring frequency of these parameters shall be once in a fortnight.) |
| 4.Noise Level Standards | ||
| 6.00 A.M. - 10.00 P.M. | 10.00 P.M. - 6.00 A.M. | |
| Noise level | Leq75 dB (A) | Leq70 dB (A) |
92. Standards for Effluents from Textile Industry
| Parameter | Concentration not to exceed, milligram per litre (mg/1), except pH |
| pH | 5.5-9.0 |
| Total suspended solids | 100 |
| Bio-chemical oxygen demand (BOD) | 30 |
| Chemical oxygen demand (COD) | 250 |
| Total residual chlorine | 1 |
| Oil and grease | 10 |
| Total chromium as Cr | 2 |
| Sulphideas S | 2 |
| Phenoliccompounds as C6H5OH | 1 |
2. The quantity of effluent (litre per kilogram of product) shall not exceed 100, 250 and 80 in composite cotton textile industry, composite woollen textile industry and textile processing industry, respectively.
93. Primary Water Quality Criteria for Bathing Waters
In a water body or its part, water is subjected to several types of uses. Depending on the types of uses and activities, water quality criteria have been specified to determine its suitability for a particular purpose. Among the various types of uses there is one use that demands highest level of water quality or purity and that is termed as "Designated Best Use" in that stretch of water body. Based on this, water quality requirements have been specified for different uses in terms of primary water quality criteria. The primary water quality criteria for bathing water are specified alongwith the rationale in Table 1.TABLE 1PRIMARY WATER QUALITY CRITERIA FOR BATHING WATER(Water used for organised outdoor bathing)| CRITERIA | RATIONALE | |
| 1. Fecal Coliform MPN/100 ml: | 500 (desirable) 2500 (Maximumpermissible) | To ensure low sewage contamination. Fecal Coliform and Fecal Streptococci are considered as they reflect the bacterial pathogenicity. |
| 2. Fecal Streptococci MPN/100ml: | 100 (desirable) 500 (Maximum permissible) | The desirable and permissible limits are suggested to allow for fluctuation in environmental conditions such as seasonal change, changes in flow conditions, etc. |
| 3. pH: | Between6.5-8.5 | The range provides protection to the skin and delicate organs like eyes, nose, ears, etc., which are directly exposed during outdoor bathing. |
| 4. Dissolved Oxygen: | 5 mg/1 or more | The minimum dissolved oxygen concentration of 5 mg/1 ensures reasonable freedom from oxygen consuming organic pollution immediately upstream which is necessary for preventing production of anaerobic gases (obnoxious gases) from sediment. |
| 5. Biochemical Oxygen demand 3 day,27oC: | 3 mg/1 or less | The Biochemical Oxygen Demand of 3 mg/1 or less of the water ensures reasonable freedom from oxygen demanding pollutants and prevents production of obnoxious gases. |
94. [ Noise Limit for Generator Sets Run with Diesel] [Inserted by G.S.R. 371(E), dated 17.5.2002 (w.e.f. 17.5.2002).]
1. Noise limit for diesel generator sets (upto 1000 KVA) manufactured on or after the [1st January, 2005] [Substituted by G.S.R. 448(E), dated 12.7.2004 (w.e.f. 12.7.2004).].
The maximum permissible sound pressure level for new diesel generator (DG) sets with rated capacity upto 1000 KVA, manufactured on or after [the 1st January, 2005] [Substituted by G.S.R. 448(E), dated 12.7.2004 (w.e.f. 12.7.2004).] shall be 75 dB(A) at 1 metre from the enclosure surface.The diesel generator sets should be provided with integral acoustic enclosure at the manufacturing stage itself.The implementation of noise limit for these diesel generator sets shall be regulated as given in paragraph 3 below.2. Noise limit for DG sets not covered by paragraph 1. Noise limits for diesel generator sets not covered by paragraph 1, shall be as follows:-
01. The manufacturer shall offer to the user a standard acoustic enclosure of 25 dB(A) insertion loss and also a suitable exhaust muffler with insertion loss of 25 dB(A).
02. The user shall make efforts to bring down the noise levels due to the DG set, outside his premises, within the ambient noise requirements by proper sitting and control measures.
03. Installation of a DG set must be strictly in compliance with the recommendations of the DG set manufacturer.
04. A proper routine and preventive maintenance procedure for the DG set should be set and followed in consultation with the DG set manufacturer which would help prevent noise levels of the DG set from deteriorating with use.
3. Limits of Noise for DG sets (upto 1000 KVA) manufactured on or after the [1st January, 2005] [Substituted by G.S.R. 448(E), dated 12.7.2004 (w.e.f. 12.7.2004).].
01. These rules apply to DG sets upto 1000 KVA rated output, manufactured or imported in India, on or after [the 1st January, 2005] [Substituted by G.S.R. 448(E), dated 12.7.2004 (w.e.f. 12.7.2004)].
02. These rules shall not apply to-
(a)DG sets manufactured or imported for the purpose of exports outside India; and(b)DG sets intended for the purpose of sample and not for sale in India.4. [0 Exemption from the provisions of paragraph 1 and 3, for the products (diesel generator sets upto 30 KVA) purchased by the Ministry of Defence, Government of India.] [Inserted by G.S.R. 315(E), dated 16.5.2005 (w.e.f. 16.5.2005).]
The products manufactured in or imported into India till [30th April, 2007] [Substituted by G.S.R. 464(E), dated 7.8.2006 (w.e.f. 7.8.2006).] for the purpose of supplying to the Ministry of Defence, shall be exempted from the regulations given in paragraphs 1 to 3 above, subject to the following conditions, namely :-5. [0 Exemption from the provisions of paragraph 1 and 3 for sixteen Diesel Generator sets of 45 KVA purchased by the Ministry of Defence, Government of India.] [Inserted by G.S.R. 566(E), dated 29.8.2007 (w.e.f. 29.8.2007).]
The 45 KVA DG sets manufactured in India for the purpose of their use in Mobile Decontamination System for use by the Ministry of Defence shall be exempted from the regulations given in paragraph 1 to 3 above subject to the following conditions, namely :-6. [0 Transportation of Diesel Generator Sets (above 250 KVA)
95. [ Emission limits for new diesel engine up to 800 kW for generator set (Genset) application.- The emission limits for new diesel engine upto 800 kW for generator set (hereinafter referred to as Genset) application [shall, in respect of the power category 'upto 19 kW', as specified in column (I) of the table below, be effective from [1st May, 2015] [Substituted by Notification No. G.S.R. 771(E) dateed by 11.12.2013 (w.e.f. 19.11.1986)], and in respect of the power categories 'more than 19 KW upto 75 KW' and 'more than 75 KW upto 800 KW, as specified in the said Table, be effective from 1st July, 2014,] [Inserted by G.S.R. 752(E), dated 24.10.2008 (w.e.f. 24.10.2008).] subject to the general conditions contained therein, namely:-
TABLE| Power Category | EmissionLimits (g/k W-hr) | Smoke Limit(light absorption coefficient, M-1) | ||
| NOx+HC | CO | PM | ||
| Upto 19 KW | _7.5 | _3.5 | _0.3 | _0.7 |
| More than 19 KWupto 75 KW | _4.7 | _3.5 | _0.3 | _0.7 |
| More than 75 KWupto 800 KW | _4.0 | _3.5 | _0.2 | _0.7 |
1. The abbreviations used in the Table shall mean as under: NOx - Oxides of Nitrogen; HC - Hydrocarbon; CO - Carbon Monoxide; and PM - Particulate Matter.
2. Smoke shall not exceed above value throughout the operating load points of the test cycle.
3. The testing shall be done as per D2 - 5 mode cycle of ISO: 8178- Part 4.
4. The above mentioned emission limits shall be applicable for Type Approval and Conformity of Production (COP) carried out by authorised agencies.
5. Every manufacturer, importer or, assembler (hereinafter referred to as manufacturer) of the diesel engine (hereinafter referred to as 'engine') for genset application manufactured or imported into India or, diesel genset (hereinafter referred to as 'product'), assembled or imported into India shall obtain Type Approval and comply with COP of their product(s) for the emission limits which shall be valid for the next COP year or, the date of implementation of the revised norms specified above, whichever earlier.
Explanation- The term 'COP year' means the period from 1st April to 31st March.6. Stack height (in metres), for genset shall be governed as per Central Pollution Control Board (CPCB) guidelines.
General Conditions1. Applicability - These conditions shall apply to all new engines for genset application and products manufactured, assembled or, imported into India, as the case may be :
Provided that these rules, shall not apply to, -2. Requirement of certification - Every manufacturer of engine or product, as the case may be, shall have valid certificate(s) of Type Approval and COP for each COP year, for all engine models being manufactured or, for all engine or product models being imported, after the effective date for the emission limits, as specified above and the COP for the genset [of the power category 'upto 19KW' sold on or after [1st May, 2015] [Substituted for the words "shall be effective from 1st July, 2014 as specified in the Table below" by Notification No. G.S.R. 789 (E) dated 11.11.2014 (w.e.f. 19.11.1986)] and of the power catogories 'more than 19kW upto 75 KW' and 'more than 75 KW upto 800 KW' sold on or after 1st July, 2014 shall be effective and in force as per revised emission norms with effect from [1st May, 2016] [Substituted for the words "1st January, 2016" by Notification No. G.S.R. 105(E) dated 17.2.2015 (w.e.f. 19.11.1986)] and 1st July, 2015, respectively].
3. Sale, import or use of engine or product not complying with these rules - No person shall sell, import or use an engine for genset application or, a product which is not having a valid Type Approval certificate and certificate of COP referred to in condition 2.
4. Requirement of conformance labeling. - (1) All the engines, individually or as part of the product shall be clearly engraved 'Genset Engine' on the cylinder block.
5. Nodal Agency. - (1) The Central Pollution Control Board shall be the nodal agency for implementation of these rules.
6. Authorised agencies for certification. - The following institutions are authorised to carry out such tests as they may deem necessary, for giving certificates of Type Approval and Conformity of Production tests for diesel engines or products and to give such certificates, namely:-
7. Compliance and testing procedure. - (1) The Compliance and Testing Procedure, as published by the Central Pollution Control Board shall be followed by all concerned.
8. Fuel Specification - The specification of commercial fuel applicable for diesel gensets shall be the same as applicable for commercial High Speed Diesel applicable for diesel vehicles in the area where product would be operated, from time to time, as per policy of Government of India.
9. Engine component or parts identification - All the details of engine components or parts responsible for the emission performance shall be clearly marked in English language.]
[Exemption from the Emission Norms for twenty Diesel Gensets of 113.2 kW to be procured by Bharat Electronics Limited for 3D Tactical Control Radar for Indian Army. [Inserted by Notification No. G.S.R. 54 (E) dated 23.1.2015 (w.e.f. 19.11.1986)]The 113.2 kW diesel gensets manufactured by M/s Kirloskar Oil Engine Limited, Pune for the purpose of their use in 3D Tactical Control Radars System for use by the Indian Army shall be exempted from the regulations specified for new diesel engine upto 800 kW for generator set, under this entry, subject to following conditions, namely:-| Power Category | Emission Limits (g/kW-hr) | |
| NOX + NMHC Or NOX + RHC | CO | |
| Upto 19 kW | ≤ 7.5 | ≤ 3.5 |
| More than 19 kW upto 75 kW | ≤ 4.7 | ≤ 3.5 |
| More than 75 kW upto 800 kW | ≤ 4.0 | ≤ 3.5 |
2. Dedicated NG or LPG genset engine shall mean a mono-fuel engine starting and operating with only one fuel, i.e., NG or LPG.
3. NOX + NMHC or NOX + RHC shall be measured in case of dedicated NG or LPG genset engine. NMHC shall be equal to 0.3×Total Hydrocarbon (THC) in case of NG, and RHC is equal to 0.5×THC in case of LPG.
4. These norms shall be applicable to Original Equipment Manufacturer (OEM) built dedicated NG or LPG genset engines.
5. The above mentioned emission limits shall be applicable for Type Approval and Conformity of Production (COP) carried out by authorised agencies.
6. Any of the following institutions shall undertake Type Approval and for verification of Conformity of Production for emission standards for engine products and to issue such certificates on compliance of the prescribed norms, namely:-
7. Stack height (in metres), for genset shall be governed as per Central Pollution Control Board (CPCB) guidelines.
B. Noise Limits. - 1. The maximum permissible sound pressure level for genset, with rated capacity upto 800 kW shall be 75 dB(A) at 1 metre from the enclosure surface. Gensets should be provided with integral acoustic enclosure at the manufacturing stage itself. The noise norms shall be effective from the 1st January, 2017.2. Noise limit for gensets not covered under paragraph (1) shall be as follows:-
3. Any of the following institutions shall undertake Type Approval and for verification of Conformity of Production for noise norms for dedicated NG or LPG gensets and issue such certificates on compliance of the prescribed norms, namely :-
2. These conditions shall apply to all new engines for genset application and products manufactured, assembled or imported into India, as the case may be:
Provided that these rules, shall not apply to, -3. Every manufacturer of engine or product, as the case may be, shall have valid certificates of Type Approval and COP for each COP year, for all engine models being manufactured or, for all engine or product models being imported, after the effective date of the emission limits, as specified above and CPCB shall develop system and procedure to monitor the norms and COP year.
4. Every manufacturer shall submit its engine or products, as the case may be, for the verification for conformity of production for emission and noise, by any of the institutions, as applicable, every COP year.
Note. - The term COP year, duty cycle and any other requirement for compliance of Type Approval and COP shall be prescribed in the system and procedure to be developed by the Central Pollution Control Board.5. No person shall manufacture, sell, import or use an engine for genset application or any product which is not having a valid Type Approval certificate and certificate of COP referred to in sub - paragraph (3) above, as applicable.
6. All the engines, individually or as part of the product shall be clearly engraved as NG genset Engine or LPG genset engine on the cylinder block, as the case may be.
7. The engine or the product shall be affixed with a conformance label meeting the following requirements, namely:-
8. The conformance label shall contain the following information, namely:-
9. (a) The Central Pollution Control Board shall be the nodal agency for implementation of these rules.
10. (a) All genset engines operating on dedicated NG or LPG shall be tested for Type Approval and COP of emission and noise limits compliance as per system and procedure published from time to time by the Central Pollution Control Board.
11. All genset engines operating on dedicated NG or LPG shall comply safety requirements.
12. The specification of commercial fuel applicable for NG or LPG shall be applicable for vehicles run on NG or LPG in the area where product shall be operated, from time to time, as per policy of Government of India.
13. All the details of engine components or part responsible for the emission performance shall be clearly marked in English language.
95B. Genset run on Petrol and Natural Gas (NG) or Petrol and Liquid Petroleum Gas (LPG):-
A. Emission Limits. - The emission limits for Petrol and NG or Petrol and LPG genset (upto 19 kW) powered by SI engine (upto 400 cc displacement) (hereinafter referred to as Genset) shall be effective from the 1st August, 2016 as specified in the following Table:-Table| Class | Engine Displacement (cc) | CO (g/kWh) | NOX + THC/ NOX + NMHC/ NOX + RHC (g/kWh) |
| 1. | Upto 99 | ≤ 250 | ≤ 12 |
| 2. | 99 and upto 225 | ≤ 250 | ≤ 10 |
| 3. | ≥225≤ 400 | ≤ 250 | ≤ 8 |
2. Dual fuel engine operation shall mean a two - fuel system having petrol as a primary combustion fuel and NG or LPG as supplementary fuel, both in a certain proportion, throughout the engine operating zone. Such dual fuel Genset engine may operate on petrol stand-alone mode in absence of gaseous fuel i.e. NG or LPG.
3. NMHC shall be equal to 0.3×THC in case of Natural Gas and RHC shall be equal to 0.5×THC in case of LPG.
4. These norms shall be applicable to Original Equipment Manufacturer (OEM) built petrol and NG or petrol and LPG genset (upto 19 kW) powered by SI engine (upto 400 cc displacement). Conversion or Retrofitment of the existing petrol or Kerosene generator sets to run on petrol and NG or petrol and LPG shall not be permitted.
5. The above emission limits shall be applicable for Type Approval and Conformity of Production (COP) undertaken by authorized agencies and shall be complied with petrol alone or petrol and NG or LPG fuel mode separately.
6. Any of the following institutions shall undertake Type Approval and for verification of Conformity of Production for emission standards for engine products and to issue such certificates on compliance of the prescribed norms, namely:-
7. NOX + THC shall be measured as emissions from petrol alone in bi-fuel fuel mode of operation. NOX + NMHC or NOX +RHC shall be measured in case of petrol and NG or petrol and LPG fuel mode of operation, respectively.
B. Noise Limits. - 1. The noise limit for gensets (upto 19 kW) powered by an SI engine (upto 400 cc displacement) run on petrol and NG or petrol and LPG shall be effective from the 1st September, 2016 as specified in the following table :-Table| Noise Parameter | Noise Limits |
| Sound Power Levelwa | 86 dB(A) |
2. Any of the following institutions shall undertake Type Approval and for verification of Conformity of Production for noise norms for dedicated petrol or petrol and NG or LPG gensets and issue such certificates on compliance of the prescribed norms, namely :-
2. These conditions shall apply to all new engines for genset application and products manufactured, assembled or imported into India, as the case may be:
Provided that these rules, shall not apply to, -3. Every manufacturer of engine or product, as the case may be, shall have valid certificates of Type Approval and COP for each COP year, for all engine models being manufactured or, for all engine or product models being imported, after the effective date of the emission limits, as specified above and CPCB shall develop system and procedure to monitor the norms and COP year.
4. Every manufacturer shall submit its engines or products to the verification for conformity of production for emission and noise, by any of the institutions, as applicable, every COP year.
Note. - The term 'COP year', duty cycle and any other requirement for compliance of Type Approval and COP to be prescribed in the System and Procedure developed by the Central pollution Control Board.5. No person shall manufacture, sell, import or use an engine for genset application or any product which is not having a valid Type Approval certificate and certificate of COP referred to in sub - paragraph (3) above, as applicable.
6. All the engines, individually or as part of the product shall be clearly engraved as petrol and NG genset Engine or petrol and LPG genset engine on the cylinder block, as the case may be.
7. The engine or the product shall be affixed with a conformance label meeting the following requirements, namely:-
8. The conformance label shall contain the following information, namely:-
9. (a) The Central Pollution Control Board shall be the nodal agency for implementation of these rules.
10. (a) All genset engines operating on petrol and NG or LPG shall be tested for Type Approval and COP of emission and noise limits compliance as per system and procedure published from time to time by the Central Pollution Control Board.
11. All genset engines operating on petrol and NG or LPG shall comply safety requirements.
12. The specification of commercial fuel applicable for petrol and NG or LPG shall be applicable for vehicles run on petrol and NG or LPG in the area where product shall be operated, from time to time, as per policy of Government of India.
13. All the details of engine components or part responsible for the emission performance shall be clearly marked in English language.
95C. Genset run on Diesel and Natural Gas (NG) or Diesel and Liquid Petroleum Gas (LPG) :-
A. Emission Limits. - The emission limits for Diesel and NG or Diesel and LPG driven engine (upto 800 kW) for generator set (hereinafter referred to as Genset) application shall be effective from the 1st July, 2016 as specified in the Table below, subject to the general conditions specified therein, namely:-Table| Power Category | Emission Limits (g/kW-hr) | Smoke Limit (light absorption coefficient,m-1) | ||
| NOX + THC or NOX + NMHCor RHC | CO | PM | ||
| Upto 19 kW | ≤ 7.5 | ≤ 3.5 | ≤ 0.3 | ≤ 0.7 |
| More than 19 kW upto 75 kW | ≤ 4.7 | ≤ 3.5 | ≤ 0.3 | ≤ 0.7 |
| More than 75 kW upto 800 kW | ≤ 4.0 | ≤ 3.5 | ≤ 0.2 | ≤ 0.7 |
2. Dual fuel engine operation shall mean a two - fuel system having diesel as a primary combustion fuel and NG or LPG as supplementary fuel, both in a certain proportion, throughout the engine operating zone. Such dual fuel genset engine may operate on diesel stand-alone mode in absence of gaseous fuel i.e. NG or LPG.
3. NOX + THC shall be measured as emission while diesel alone is used as fuel. NOX + NMHC or NOX + RHC shall be measured in case of diesel and NG or diesel and LPG dual fuel operation respectively. NMHC shall be equal to 0.3 × THC in case of NG and RHC as 0.5 × THC in case of LPG.
4. These norms shall be applicable to Original Equipment Manufacturer (OEM) built diesel and NG or LPG Genset engines. Conversion or retro fitment of the existing diesel engines to run on diesel and NG or diesel and LPG shall not be permitted.
5. The above mentioned emission limits shall be applicable for Type Approval and Conformity of Production (COP) carried out by authorised agencies. For Type Approval and COP for diesel and NG or diesel and LPG dual fuel operation engines, the emission and smoke limits prescribed in above Table shall be met in diesel alone or diesel and NG or diesel and LPG dual fuel mode separately.
6. Any of the following institutions shall undertake Type Approval and for verification of Conformity of Production for emission standards for engine products and to issue such certificates on compliance of the prescribed norms, namely:-
7. Stack height (in metres) for genset shall be governed as per Central Pollution Control Board (CPCB) guidelines.
8. NOX + THC shall be measured as emissions from diesel alone in bi-fuel fuel mode of operation. NOX + NMHC or NOX +RHC shall be measured in case of diesel and NG or diesel and LPG fuel mode of operation, respectively.
9. The emission standards for smoke and particulate matter shall be applicable, when diesel is used as fuel. Smoke limit prescribed in above Table shall not exceed throughout the operating load points of the test cycle.
B. Noise Limits. - 1. The maximum permissible sound pressure level for genset, with rated capacity upto 800 kW shall be 75 dB(A) at 1 metre from the enclosure surface. Gensets shall be provided with integral acoustic enclosure at the manufacturing stage itself. The noise norms shall be effective from the 1st January, 2017.2. Noise limit for gensets not covered under paragraph (1) shall be as follows:-
3. Any of the following institutions shall undertake Type Approval and for verification of Conformity of Production for noise norms for dedicated diesel or diesel and NG or LPG gensets and issue such certificates on compliance of the prescribed norms, namely :-
2. These conditions shall apply to all new engines for genset application and products manufactured, assembled or imported into India, as the case may be:
Provided that these rules, shall not apply to, -3. Every manufacturer of engine or product, as the case may be, shall have valid certificates of Type Approval and COP for each COP year, for all engine models being manufactured or, for all engine or product models being imported, after the effective date of the emission limits, as specified above and CPCB shall develop system and procedure to monitor the norms and COP year.
4. Every manufacturer shall submit its engine or products, as the case may be, for the verification of conformity of production for emission and noise, by any of the institutions, as applicable, every COP year.
Note. - The term COP year, duty cycle and any other requirement for compliance of Type Approval and COP shall be prescribed in the system and procedure to be developed by the Central Pollution Control Board.5. No person shall manufacture, sell, import or use an engine for genset application or any product which is not having a valid Type Approval certificate and certificate of COP referred to in sub - paragraph (3) above.
6. All the engines, individually or as part of the product shall be clearly engraved as diesel and NG genset Engine or diesel and LPG genset engine on the cylinder block, as the case may be.
7. The engine or the product shall be affixed with a conformance label meeting the following requirements, namely:-
8. The conformance label shall contain the following informations, namely:-
9. (a) The Central Pollution Control Board shall be the nodal agency for implementation of these rules;
10. (a) All genset engines operating on diesel and NG or LPG shall be tested for Type Approval and COP of emission and noise limits compliance as per system and procedure published from time to time by the Central Pollution Control Board.
11. All genset engines operating on diesel and NG or LPG shall comply safety requirements.
12. The specification of commercial fuel applicable for diesel and NG or LPG shall be applicable for vehicles run on diesel and NG or LPG in the area where product shall be operated, from time to time, as per the policy of the Government of India.
13. All the details of engine components or part responsible for the emission performance shall be clearly marked in English language.] [Inserted by Notification No. G.S.R. 281(E), dated 7.3.2016 (w.e.f. 19.11.1986).]
96. [ [Inserted by G.S.R. 489(E), dated 9.7.2002 (w.e.f. 11.7.2002).] Emission Standards for Diesel Engines (Engine rating more than 0.8 MW (800 KW) for Power Plant, Generator Set Applications and other Requirements.] [Inserted by G.S.R. 640(E), dated 16.10.2006 (w.e.f. 16.10.2006).]
TABLE| Parameter | Area Category | Total engine rating of the plant (includes existing as well as new generator sets) | Generator sets commissioning date | ||
| Before 1-7-2003 | Between 1-7-2003 and 1-7-2005 | On or after 1-7-2005 | |||
| NOx(as NO2) (at 15% 02), dry basis, in ppmv | A | Upto 75 MW | 1100 | 970 | 710 |
| B | Upto 150 MW | ||||
| A | More than 75 MW | 1100 | 710 | 360 | |
| B | More than 150 MW | ||||
| NMHC (as C) (at 15% O2), mg/Nm3 | Both A and B | 150 | 100 | ||
| PM (at 15% 02), mg/Nm3 | Diesel Fuels-HSD and LDO | Both A and B | 75 | 75 | |
| Furnace Oils-LSHS and FO | Both A and B | 150 | 100 | ||
| CO (at 15% O2), mg/Nm3Both A and B | 150 | 150 | |||
| Sulphurcontent in fuel | A | 2% | |||
| B | 4% | ||||
| Fuel specification | For A only | Upto5 MW | Only Diesel Fuels (HSD, LDO) shall be used. | ||
| Stack height (for generator sets commissioned after 1-7-2003) | Stack height shall be maximum of the following, in metre: | ||||
| (i) 14 Q0.3, Q=Total SO2emission from the plant in kg /hr. | |||||
| (ii) Minimum 6 m. above the building where generator set is installed, | |||||
| (iii) 30 m. |
| Note.- | |||
| 1. Acronyms used: | |||
| MW . | Mega (106) Watt | FO | Furnace Oil |
| NOx | Oxides of Nitrogen | HSD | High Speed Diesel |
| NO2 | Nitrogen Dioxide | LDO | Light Diesel Oil |
| O2 | Oxygen | LSHS | LowSulphurHeavy Stock |
| NMHC | Non-Methane Hydrocarbon | kPa | Kilo Pascal |
| C | Carbon | mm | Milli(10-3) metre |
| PM | Particulate Matter | kg/hr | Kilo (103) gram per hour |
| CO | Carbon Monoxide | mg/Nm3 | Milli(10-3) gram per normal metre cubic |
| SO2ppmv | SulphurDioxide part per million (106) by volume |
2. Area categories A and B are defined as follows:
Category A: Areas within the municipal limits of towns/cities having population more than 10 lakhs and also upto 5 km beyond the municipal limits of such town/cities.Category B: Areas not covered by category A.3. The standards shall be regulated by the State Pollution Control Boards or Pollution Control Committees, as the case may be.
4. Individual units with engine ratings less than or equal to 800 KW are not covered by this notification.
5. Only following liquid fuels, viz., High Speed Diesel, Light Diesel Oil, Low Sulphur Heavy Stock and Furnace Oil or liquid fuels with equivalent specifications shall be used in these power plants and generator sets.
6. For expansion project, stack height of new generator sets shall be as per total Sulphur Dioxide emission (including existing as well as additional load).
7. For multi-engine plants, fuels shall be grouped in cluster to get better plume rise and dispersion. Provision for any future expansion should be made in planning stage itself.
8. Particulate matter, Non-Metharie Hydrocarbon and Carbon Monoxide results are to be normalised to 25°C, 1.01 Kilo Pascal (760 mm of mercury) pressure and zero percent moisture (dry basis).
9. Measurement shall be performed at steady load conditions of more than 85% of the rated load.
10. Continuous monitoring of Oxides of Nitrogen shall be done by the plants whose total engine capacity is more than 50 Mega Watt. However, minimum once in six month monitoring for other parameters shall be adopted by the plants.
11. Following methods may adopted for the measurement of emission parameters,-
| Sl. No. | Emissionparameters | Measurement methods | |
| 1. | Particulates | Gravimetric | |
| 2. | SO2 | Barium Perchlorate-Thorin indicator method | |
| 3. | NOx | Chemiluminescence, Non-Dispersive Infra Red, Non-Dispersive Ultraviolet (for continuous measurement), Phenol disulphonic method | |
| 4. | CO | Non-Dispersive Infra Red | |
| 5. | O2 | Paramagnetic, Electrochemical sensor | |
| 6. | NMHC | Gas Chromatograph-Flame lonisation Detector]. | |
| 97. [] [Added by G.S.R. 546(E), dated 30.8.2005 (w.e.f. 30.8.2005).] | Boilers Using Agriculture Waste as Fuel | Step Great Particulate matter | 250mg/Nm3 |
| Horse Shoe/Pulsating | 500mg/Nm3 | ||
| Particulate matter | (12%of C02) | ||
| Spreader stroker | 500mg/Nm3 | ||
| Particulate matter | (12%of C02); |
98. Guidelines for Pollution Control in Ginning Mills.-
Measures for Noise Control-| Sl. No. | Industry | Parameter | Standards | ||
| 1 | 2 | 3 | 4 | ||
| 99. [] | Sponge IronPlant (Rotary Kiln) | A. EmissionStandards* | |||
| Particulatematter | Fuel Type | Limitingvalue for concentration | |||
| coal | 100 mg/Nm3 | ||||
| gas | 50 mg/Nm3 | ||||
| CarbonMonoxide (Vol./Vol.) | coal/gas | 1% | |||
| StackHeight** (minimum) | coal/gas | 30.0m | |||
| Note.-*Emissionshall be normalised at 12% CO2in stack emission. | |||||
| **Stackheight shall be calculated as H=14.0Q0.3where Q isemission of Sulphur Dioxide (SO2) in kg. /hr. i.e. | |||||
| SO2(kg/hr) | Height(metre) | ||||
| up to 12.68 | 30 | ||||
| 12.69-33.08 | 40 | ||||
| 33.09-69.06 | 50 | ||||
| 69.07-127.80 | 60 | ||||
| 127.81-213.63 | 70 | ||||
| (De-dustingunit) | Particulatematter | Existing unit | New unit | ||
| mg/Nm3 | 100 | 50 | |||
| Note. -(i) Stack attached to de-dusting unit shall have minimum heightof 30.0 metre. | |||||
| (ii) If,De-dusting unit is connected to After Burner Chamber (ABC),emission shall be emitted through common stack (minimum height30.0 metre) having separate arrangements for emission monitoringfor de-dusting unit. | |||||
| B. FugitiveEmission Standards | |||||
| Rotary Kiln/De-dusting unit | Particulatematter | Existing unit | New unit | ||
| (µg/m3) | 3000 | 2000 | |||
| Note.-(i) The existing industry shall comply with a standard of 2000(µg/m3) after one year from the date ofnotification. | |||||
| (ii) Fugitiveemission shall be monitored at a distance 10.0 metre from thesource of fugitive emission as per following: | |||||
| Area | Monitoringlocation | ||||
| Raw materialhandling area | Wagontippler, Screen area, Transfer points, Stock bin area | ||||
| Crusherarea | Crushingplant, Vibrating screen, Transfer points | ||||
| Raw materialfeed area | Feeder area,Mixing area, Transfer points | ||||
| Coolerdischarge area | Oversizedischarge area, Transfer points, Intermediate stock bin area,Screening plant, Magnetic separation unit, Transfer points, Oversize discharge area, Product separation area, Bagging area | ||||
| Productprocessing area | Intermediatestock bin area, Screening plant, Magnetic separation unit,Transfer points, Over size discharge area, Product separationarea, Bagging area | ||||
| Other areas | As specifiedby State Pollution Control Board/Pollution Control Committee | ||||
| C. EffluentStandards | |||||
| pH | 5.5-9.0 | ||||
| Totalsuspended solids | 100 mg/1 | ||||
| Oil andgrease | 10mg/1 | ||||
| Chemicaloxygen demand | 250 mg/1 | ||||
| Note.-(i) All efforts shall be made to reuse and re-circulate the waterand to maintain "Zero discharge". | |||||
| (ii) Stormwater drain shall be provided within the premises of the industryso as to avoid mixing with effluent. | |||||
| 100. [] | CommonHazardous Waste Incinerator | A. EmissionLimiting concentration in mg/Nm3, unless stated | SamplingDuration in (minutes) unless stated | ||
| ParticulateMatter | 50 | 30 | |||
| HCI | 50 | 30 | |||
| SO2 | 200 | 30 | |||
| CO | 100 | 30 | |||
| 50 | 24 hours | ||||
| Total OrganicCarbon | 20 | 30 | |||
| HF | 4 | 30 | |||
| NOx (NO andNO2expressed as NO2) | 400 | 30 | |||
| Total dioxinsand furans | 0.1 ngTEQ/Nm3 | 8 hours | |||
| Cd+Th+theircompounds | 0.05 | 2 hours | |||
| Hg and itscompounds | 0.05 | 2 hours | |||
| Sb+As+Pb+Co+Cr+Cu+Mn+Ni+V+their compounds | 0.50 | 2 hours | |||
| Notes. - | |||||
| (i) Allmonitored values shall be corrected to 11% oxygen on dry basis. | |||||
| (ii) The CO2concentration in tail gas shall not be less than 7%. | |||||
| (iii) Incase, halogenated organic waste is less than 1% by weight ininput waste, all the facilities in twin chamber incineratorsshall be designed to achieve a minimum temperature of 950°Cin secondary combustion chamber and with a gas residence time insecondary combustion chamber not less than 2 (two) seconds. | |||||
| (iv) In casehalogenated organic waste is more than 1% by weight in inputwaste, waste shall be incinerated only in twin chamberincinerators and all the facilities shall be designed to achievea minimum temperature of 1100°C in secondary combustionchamber with a gas residence time in secondary combustion chambernot less than 2 (two seconds). | |||||
| (v)incineration plants shall be operated (combustion chambers) withsuch temperature, retention time and turbulence, as to achieveTotal Organic Carbon (TOC) content in the slag and bottom ashesless than 3%, or their loss on ignition is less than 5% of thedry weight. | |||||
| 101. [] | Incineratorfor Pesticide Industry | A. EmissionLimiting concentration in mg/Nm3, unless stated | SamplingDuration in (minutes) unless stated | ||
| ParticulateMatter | 50 | 30 | |||
| HCL | 50 | 30 | |||
| SO2 | 200 | 30 | |||
| CO | 100 | daily average | |||
| Total OrganicCarbon | 20 | 30 | |||
| Total Dioxinsand Furans* | ExistingIncinerator | 0.2 ngTEQ/Nm3 | 8 hours | ||
| NewIncinerator | 0.1 ngTEQ/Nm3 | 8 hours | |||
| Sb + As + Pb+ Cr + Co + Cu + Mn + Ni + V + their compounds | 1.5 | 2hours | |||
| *The existingplant shall comply with norms for dioxins and furans as 0.1ng/TEQ/Nm3within a period of five years from the dateof publication of this notification. | |||||
| Notes.- | |||||
| (i) Allmonitored values shall be corrected to 11% oxygen on dry basis. | |||||
| (ii) The CO2concentration in tail gas shall not be less than 7%. | |||||
| (iii) Incase, halogenated organic waste is less than 1% by weight ininput waste, all the facilities in single chamber incineratorsshall be designed so as to achieve a minimum temperature of1100°C, in the incinerator. For fluidized bed technologyIncinerator, temperature shall be maintained at 950°C. | |||||
| (iv) In casehalogenated organic waste is more than 1% by weight in inputwaste, waste shall be incinerated only in twin chamberincinerators and all the facilities shall be designed to achievea minimum temperature of 1100°C in secondary combustionchamber with a gas residence time in secondary combustion chambernot less than two seconds. | |||||
| (v) Scrubbermeant for scrubbing emissions shall not be used as quencher. | |||||
| (vi)Incineration plants shall be operated (combustion chambers) withsuch temperature, retention time and turbulence, as to achieveTotal Organic Carbon (TOC) content in the slag and bottom ashesless than 3%, and their loss on ignition is less than 5% of thedry weight. | |||||
| (vii) Theincinerators shall have a chimney of atleast thirty metre height. | |||||
| B. Wastewater | |||||
| (i)Wastewater (scrubber water and floor washings) shall bedischarged into receiving water conforming to the normsprescribed under Schedule VI: General Standards for Discharge ofEnvironment Pollutions (Part A: Effluents) notified under theEnvironment (Protection) Rules, 1986. | |||||
| (ii) Thebuilt up in Total Dissolved Solids (TDS) in wastewater of floorwashings shall not exceed 1000 mg/l over and above the TDS of rawwater used. | |||||
| 102. [] | RefractoryIndustry | A. EmissionStandards | |||
| (Q Down DraftKiln (Fuel: Coal) | Category* | Limitingconcentration (mg/Nm3) | |||
| Particulatematter | small/medium/large | 350 | |||
| Minimum(metres) | |||||
| Stack height | small | 15 | |||
| medium | 18 | ||||
| large | 21 | ||||
| (ii) Otherthan Down Draft Kiln (Fuel: Coal) | |||||
| Category* | Limitingconcentration (mg/Nm3) | ||||
| ParticulateMatter | small | 300 | |||
| medium | 200 | ||||
| large | 150 | ||||
| Minimum(metres) | |||||
| Stack height | small | 15 | |||
| medium | 18 | ||||
| large | 21 | ||||
| (iii) Box,Tunnel, Down Draft Kiln, etc. (Fuel: Natural Gas/Producer Gas/LPGor a combination of Fuels/Furnance Oil as Secondary Fuel) | |||||
| Category* | Limitingconcentration (mg/Nm3) | ||||
| ParticulateMatter | small | 200 | |||
| Medium/ | 150 | ||||
| large | |||||
| Minimum(metres) | |||||
| Stack height | small | 12 | |||
| medium | 15 | ||||
| large | 18 | ||||
| Category* | Production(tpa) | ||||
| small kiln | 15,000 | ||||
| medium kiln | 15,001-50,000 | ||||
| large kiln | above 50,000 | ||||
| (iv) RotaryKiln (Fuel: Furnance Oil) | |||||
| Category** | Limitingconcentration (mg/Nm3) | ||||
| ParticulateMatter | small | 200 | |||
| Medium/ | 150 | ||||
| large | |||||
| Minimum(metres) | |||||
| Stack height | small | 35 | |||
| medium | 45 | ||||
| large | 60 | ||||
| Category** | Production(tpa) | ||||
| small rotarykiln | 50 | ||||
| medium rotarykiln | 51-100 | ||||
| large rotarykiln | above 100 | ||||
| Notes.- | |||||
| (i) Allvalues of particulate matter are to be corrected at 6 per centCarbon Dioxide. | |||||
| (ii) Fugitiveemission shall not exceed 10 mg/m3from any process orplant. | |||||
| (iii) Eachstack shall be at least 2 metre above the top most point of thebuilding, shed or plant in the industry excluding bucketelevator, mill house and vibrating screen. | |||||
| (iv) If morethan one kiln is connected to single stack, sum of the productioncapacity of all the kilns would be considered for determining thecapacity of the kiln and accordingly depending upon the totalcapacity, emission standard and stack height would beimplemented. | |||||
| (v)Monitoring of stack shall be carried out at the time of chargingand after the completion of charging and average of these tworesults shall be considered as emission level. | |||||
| B. EffluentStandards | |||||
| Limitingvalue for concentration | |||||
| InlandSurface Water | PublicSewer | Landfor Irrigation | |||
| pH | 5.5to 9.0 | 5.5to 9.0 | 5.5to 9.0 | ||
| Oil andGrease | 10 | 20 | 10 | ||
| BOD 3 days,27oC | 30 | 250 | 100 | ||
| COD | 250 | - | - | ||
| SuspendedSolids | 100 | 600 | 200 | ||
| Phenols | 1.0 | 5.0 | - | ||
| Cyanide as CN | 0.2 | 2.0 | 0.2 | ||
| Cr(Hexavalent) | 0.1 | 2.0 | 1.0 | ||
| Cr (Total) | 2.0 | 2.0 | 2.0. | ||
| [***] | |||||
| 103. [] | Cashew SeedProcessing Industry | A-Emission Standards | |||
| Process | Limitingconcentration (mg/Nm3) | ||||
| Particulatematter | Roasting | 250 | |||
| Cooking(roasted shell/deoiled cake as fuel) | 150 | ||||
| Borma OvenHeater (roasted shell/ deoiled cake as fuel) | 150 | ||||
| Stack height | minimum(metres) | ||||
| Roasting | 20 | ||||
| Cooking | 15 | ||||
| Borma OvenHeater | 15 | ||||
| Note:Allvalues of particulate matter shall be corrected at 4% CarbonDioxideEachstack shall be at least 2 metres above the top most point of thebuilding, shed or plant in the industry.Theemissions from 'Dog-house' shall be channelised alongwithRoasting-drum emissions and shall pass through wet scrubberBio-gasifiershall be installed if roasted shells are used as fuel in theunit. | |||||
| B-Effluentstandards | |||||
| Limitingconcentration in mg/l, except for pH | |||||
| Inlandsurface Water | Publicsewer | LandFor Irrigation | |||
| pH | 6.5to 8.5 | 6.5to 8.5 | 6.5to 8.5 | ||
| OilGrease | 10 | 20 | 10 | ||
| BOD 3 days,270c | 30 | 250 | 100 | ||
| SuspendedSolids | 100 | 600 | 200 | ||
| Phenols | 1 | 5 |
| Sl. No. | Industry | Parameters | Standards | |
| 1 | 2 | 3 | 4 | |
| Effluent discharge standards (applicable to all mode ofdisposal) | ||||
| 105. [ [Inserted by Notification No. G.S.R. 1265(E), dated 13.10.2017 (w.e.f. 19.11.1986).] | Sewage Treatment Plants (STPs) | Location | Concentration not to exceed | |
| (a) | (b) | |||
| pH | Anywhere in the country | 6.5-9.0 | ||
| Bio-Chemical Oxygen Demand (BOD) | Metro Cities*, all State Capitals except in theState of Arunachal Pradesh, Assam, Manipur, Meghalaya Mizoram,Nagaland, Tripura Sikkim, Himachal Pradesh, Uttarakhand, Jammuand Kashmir, and Union territory of Andaman and Nicobar Islands,Dadar and Nagar Haveli Daman and Diu and Lakshadweep | 20 | ||
| Areas/regions other than mentioned above | 30 | |||
| Total Suspended Solids (TSS) | Metro Cities*, all State Capitals except in theState of Arunachal Pradesh, Assam, Manipur, Meghalaya Mizoram,Nagaland, Tripura Sikkim, Himachal Pradesh, Uttarakhand, Jammuand Kashmir and Union territory of Andaman and Nicobar Islands,Dadar and Nagar Haveli Daman and Diu and Lakshadweep | 50 | ||
| Areas/regions other than mentioned above | 100 | |||
| Fecal Coliform (FC) (Most Probable Number per100 milliliter, MPN/100ml | Anywhere in the country | 1000 | ||
| *Metro Cities areMumbai, Delhi, Kolkata, Chennai, Bengaluru, Hyderabad, Ahmedabadand Pune.Note:(i) All values inmg/l except for pH and Fecal Coliform.(ii) These standardsshall be applicable for discharge into water bodies as well asfor land disposal/applications.(iii) The standardsfor Fecal Coliform shall not apply in respect of use of treatedeffluent for industrial purposes.(iv) These Standardsshall apply to all STPs to be commissioned on or after the 1stJune, 2019 and the old/existing STPs shall achieve thesestandards within a period of five years from date of publicationof this notification in the Official Gazette.(v) In case ofdischarge of treated effluent into sea, it shall be throughproper marine outfall and the existing shore discharge shall beconverted to marine outfalls, and in cases where the marineoutfall provides a minimum initial dilution of 150 times at thepoint of discharge and a minimum dilution of 1500 times at apoint 100 meters away from discharge point, then, the existingnorms shall apply as specified in the general dischargestandards.(vi) Reuse/Recyclingof treated effluent shall be encouraged and in cases where partof the treated effluent is reused and recycled involvingpossibility of human contact, standards as specified above shallapply.(vii) Central Pollution Control Board/StatePollution Control Boards/Pollution Control Committees may issuemore stringent norms taking account to local condition undersection 5 of the Environment (Protection) Act, 1986;.] |
| [Sl. No. [Inserted by Notification No. G.S.R. 263 (E), dated 22.3.2018 (w.e.f. 19.11.1986).] | Type of Industrial Sector | Standards | |
| SO2(mg/Nm3) | NOx(mg/Nm3) | ||
| 107 | Ceramic* | 400 | 600 |
| 108 | Foundry Industries ** (Furnaces based on Fuel) | 300 | 400 |
| 109 | Glass*** | 500 for natural gas firing 1500 for other fuels | 1000 |
| 110 | Lime Kiln**** | 400 | 500 |
| 111 | Reheating furnace***** | 300 | 1000] |
| Sl. No. | Industry | Parameters | Standards |
| 1 | 2 | 3 | 4 |
| Ambient Air Quality Standards with respect toNoise in Airport Noise Zone | |||
| [112 [Inserted by Notification No. G.S.R. 568(E), dated 18.6.2018 (w.e.f. 19.11.1986).] | Airports | Type of Airports | Limits in dB (A) Leq* |
| Day Time | Night Time | ||
| Busy Airports | 70 | 65 | |
| All other Airports excluding proposed airports | 65 | 60] | |
| [113 [Inserted by Notification No. G.S.R. 5(E), dated 3.1.2019 (w.e.f. 19.11.1986.).] | Kerosene standards | Characteristic | Requirement |
| Grade A | Grade B | ||
| Appearance | Clear and bright, Free from un-dissolved water,foreign matter and other visible impurities | Clear and bright, Free from un-dissolved water,foreign matter and other visible impurities | |
| Acidity, inorganic | Nil | Nil | |
| Burning quality(2) | |||
| (a) Char value, mg/Kg of oil consumed,Max | 20 | 20 | |
| (b) Bloom on glass Chimney | Not darkar than grey | No darkar than grey | |
| Colour | |||
| (a) Saybolt (in case of undyed kerosene)(3),Min | 10 | 10 | |
| (b) Visual (in case of dyed kerosene) | Blue | Blue | |
| Copper strip corrosion for 3 h at 500C | Not worse than No. 1 | Not worse than No. 1 | |
| Density at 150C, kg/m3 | Not limited, but to be reported | Not limited, but to be reported | |
| Distillation | |||
| (a) Percent recovered below 2000C, percent(v/v),Min | 20 | 20 | |
| (b) Final boiling point,0C,Max | 300 | 300 | |
| Flash point (Abel),0C,Min | 35 | 35 | |
| Smoke point(4), mm,Min | 18 | 18 | |
| Total sulphur content, percent(5)m/m,Max | 0.10 | 0.20* | |
| *The Ministry of Petroleum and Natural Gas shallmake efforts to produce and supply Grade A kerosene by 2020 | |||
| Notes:(1) In case of dispute, this shall be the referee method.(2) This test is to be done at refinery end.(3) Where Saybolt chromo meter is not available Lovibond colour of the sample kept in an 18 cell may be measured according to IS 1448: P-13 in which case the colour shall not be deeper than standard white (IP 4.0), however, in case of dispute [P:14] shall be referee method.(4) For supplies to Defence and Railway signal lamps the smoke point of the product shall be 22 mm, Minimum.(5) For all other specifications i.e. test methods, scope, references, grades, requirements, packing and marketing and sampling. It is require to meet Indian Standard IS 1459:2018 for Kerosene Specifications (Fourth Revision), ICS No. 75.160.20, published in July, 2018] |
1.
2. Compliance of noise levels applicable to Airport Noise Zone as specified above shall lie with the airport operator and overseen by the Directorate General of Civil Aviation.
3. Airport operators shall prepare Noise Management Plan for compliance of the Airport Noise Standards.
4. Airport Noise Zones. - (1) The Airport Noise Zone area for each Airport shall be defined as Noise Contour for day and night period by the respective Airport Operator on the basis of existing GSR 751 (E), issued by the Ministry of Civil Aviation (Height Restrictions for Safeguarding of Aircraft Operations) Rules, 2015 published on 30th September, 2015 as amended from time to time on Height Restriction for Safeguarding of Aircraft Operation considering all approach and departure funnels and Instrument Flight Procedures (i.e. Instrument Approach Procedures, Standard Instrument Departure Standard Terminal Arrival Route) in consultation with airports Air Navigation Service Provider as per the Master Plan of the Airport. The same shall be shall be approved by the Directorate General of Civil Aviation and displayed on the website of respective Airport Operators. This activity shall be completed within two years from the date of issuance of the final notification.
5. Airport Noise Mapping. - Noise mapping in for all airports should be carried out as per the requirements specified in the Director General Civil Aviation's requirements by the airport operators considering future aircraft movement and traffic projections of the airport as per the Master Plan of the Airport. This information to be displayed at a prominent places at Airports as well as in the website of respective Airport Operator and State / Union Territory Development Authority.
6. Protocol and Measurements Procedure. - Monitoring protocol and measurements procedure for airport noise zone displayed on the website of the Ministry of Environment, Forest and the Climate Change and the Central Pollution Control Board shall be followed.
7. Development Authorities / Regional Planning Department shall specify provisions for inclusion of sound resistance in new buildings, facilities and projects of residential, institutional, hospital and commercial facilities in the design, construction and materials selections for improving indoor environment under existing building codes and bye laws for any building constructions coming under airport noise zones.
8. All the Airport, Airline and Authority shall comply with the requirements specified in the notification within two years from the date of notification.]
[SCHEDULE III] [Inserted by G.S.R. 1063(E), dated 26.12.1989 (w.e.f. 26.12.1989).](See rule 3)AMBIENT AIR QUALITY STANDARDS IN RESPECT OF NOISE| Area Code | Category of Area | Limits in dB(A) | Leg. |
| Day Time | Night Time | ||
| (A) | Industrial area | 75 | 70 |
| (B) | Commercial area | 65 | 55 |
| (C) | Residential area | 55 | 45 |
| (D) | Silence Zone | 50 | 40 |
| Method of Test | Maximum smoke density | ||
| Light absorption co-efficient m-1 | Bosch Units | Hatridge Units | |
| (a) Full load at a speed of 60% to 70% of maximum engine rated speed declared by the manufacturer | 3.1 | 5.2 | 75 |
| (b) Free acceleration | 2.3 | - | 65 |
| Mass of Carbon Monoxide (CO) Maxm.Grams per KWH | Mass of Hydro Carbons (HC) Maxm.Grams per KWH | Mass of Nitrogen Oxides (NO) Maxm.Grains per KWH |
| 14 | 3.5 | 18 |
1. Type Approval Tests:
Two and Three Wheeler Vehicles| Reference Mass, R(kg) | CO(g/km) | HC(G/km) | ||
| 1 | 2 | 3 | ||
| R≤ 150 | 12 | 8 | ||
| 150R≤ 350 | 12+ | 18(R-150)200 | 8+ | 4(R-150)200 |
| R350 | 30 | 12 |
| Reference Mass, rw(kg) | CO(g/km) | HC(g/km) |
| 1 | 2 | 3 |
| rw ≤ 1020 | 14.3 | 2.0 |
| 1020 rw≤ 1250 | 16.5 | 2.1 |
| 1250 rw≤ 1470 | 18.8 | 2.1 |
| 1470 rw≤ 1700 | 20.7 | 2.3 |
| 1700 rw≤ 1930 | 22.9 | 2.5 |
| 1930 rw≤ 2150 | 24.9 | 2.7 |
| rw≤ 2150 | 27.1 | 2.9 |
2. Conformity of Productioan Tests :
Two and Three Wheeler Vehicles| Reference Mass, rw(kg) | CO(g/km) | HC(G/km) | ||
| 1 | 2 | 3 | ||
| R150 | 15 | 8 | ||
| 150R≤ 350 | 15+ | 25(R-150)200 | 10+ | 5(R-150)200 |
| R350 | 40 | 15 |
| Reference Mass, rw(kg) | CO(g/km) | HC(g/km) |
| 1 | 2 | 3 |
| rw ≤ 1020 | 17.3 | 2.7 |
| 1020rw≤ 1250 | 19.7 | 2.7 |
| 1250rw≤ 1470 | 22.5 | 2.8 |
| 1470rw≤ 1700 | 24.9 | 3.0 |
| 1700rw≤ 1930 | 27.6 | 3.3 |
| 1930rw≤ 2150 | 29.9 | 3.5 |
| rw≤ 2150 | 32.6 | 3.7 |
| No. of Operation | Acceleration (m/acc2) | Speed (km/h) | Duration of each operation(s) | Cumulative Time(s) | |
| 1 | 2 | 3 | 4 | 5 | |
| 1. | Idling | - | - | 16 | 16 |
| 2. | Acceleration | 0.65 | 0-14 | 6 | 22 |
| 3. | Acceleration | 0.56 | 14-22 | 4 | 26 |
| 4. | Deceleration | -0.63 | 22-13 | 4 | 30 |
| 5. | Steady speed | - | 13 | 2 | 32 |
| 6. | Acceleration | 0.56 | 13-23 | 5 | 37 |
| 7. | Acceleration | 0.44 | 23-31 | 5 | 42 |
| 8. | Deceleration | -0.56 | 31-25 | 3 | 45 |
| 9. | Steady speed | - | 25 | 4 | 49 |
| 10. | Deceleration | -0.56 | 25-21 | 2 | 51 |
| 11. | Acceleration | 0.45 | 21-34 | 8 | 59 |
| 12. | Acceleration | 0.32 | 34-42 | 7 | 66 |
| 13. | Deceleration | -0.46 | 42-37 | 3 | 69 |
| 14. | Steady speed | - | 37 | 7 | 76 |
| 15. | Deceleration | -0.42 | 34-34 | 2 | 78 |
| 16. | Acceleration | 0.32 | 34-42 | 7 | 85 |
| 17. | Deceleration | -0.46 | 42-47 | 9 | 94 |
| 18. | Deceleration | -0.52 | 27-14 | 7 | 101 |
| 19. | Deceleration | -0.56 | 14-00 | 7 | 108 |
| Sl. No. | Characteristic | Requirements | Method of Test ref. of P: or IS: 1448* | |
| 87 Octane | 93 Octane | |||
| 1 | 2 | 3 | 4 | 5 |
| 1. | Colour, visual | Orange | Red | |
| 2. | Copper-strip corrosion for 3 hours at 50°C | Not worse than No.1 | P:15(1968) | |
| 3. | Density at 151C | Not limited but to be reported | P:16(1967) | |
| 4. | Distillation: | P:18(1967) | ||
| (a) Initial boiling point | Not limited but to be reported | |||
| (b) Recovery up to 20°C per cent by volume, Min. | 10 | 10 | ||
| (c) Recovery upto 125" C 50 per cent by volume | 50 | 50 | ||
| (d) Recovery upto 130°C per cent by volume, Min. | 90 | 90 | ||
| (e) Final boiling point, Max. | 215°C | 215°C | ||
| (f) Residue per cent by volume, Max. | 2 | 2 | ||
| 5. | Octane number (Research method) Max. | 87 | 94 | P:27 (1960) |
| 6. | Oxidation stability in minutes, Min. | 360 | 360 | P:28 (1966) |
| 7. | Residue on evaporation mg/100 ml, Max. | 4.0 | 4.0 | P:29 (1960) |
| (Air-jet solvent washed) | ||||
| 8. | Sulphur, total, per cent by weight Max. | 0.25 | 0.20 | P:34 (1966) |
| 9. | Lead content (as Pb), g/1 Max. | 0.56 | 0.80 | P:37 (1967) or |
| P:38 (1967) | ||||
| 10. | Reid vapour pressure at 38 degree C, kgf/cm3, Max. | 0.70 | P:39 (1967) |
| Nominal Flow G(1 /s) | Absorption Co-efficient K(m-1) | Nominal Flow G(1 /s) | Absorption Co-efficient K(m-1) |
| 42 | 2.00 | 120 | 1.20 |
| 45 | 1.91 | 125 | 1.17 |
| 50 | 1.82 | 130 | 1.15 |
| 55 | 1.75 | 135 | 1.31 |
| 60 | 1.68 | 140 | 1.11 |
| 65 | 1.61 | 145 | 1.09 |
| 70 | 1.56 | 150 | 1.07 |
| 75 | 1.50 | 155 | 1.05 |
| 80 | 1.46 | 160 | 1.04 |
| 85 | 1.41 | 165 | 1.02 |
| 90 | 1.38 | 170 | 1.01 |
| 95 | 1.34 | 175 | 1.00 |
| 100 | 1.31 | 180 | 0.99 |
| 105 | 1.27 | 185 | 0.97 |
| 110 | 1.25 | 190 | 0.96 |
| 115 | 1.22 | 195 | 0.95 |
| 20(1 | 0.93 |
| Sl. No. | Place at which the discharge of any environment pollutant in excess of prescribed standards occurs or is apprehended to occur | Authorities or agencies to be intimated | Appointed under |
| 1 | 2 | 3 | 4 |
| 1. | Factories as defined under the Factories Act, 1948 - | ||
| (a) Owned by the Central Government and engaged in carrying out the purposes of the Atomic Energy Act, 1962 | (i) Atomic Energy Regulatory | The Atomic Energy Act, 1962 | |
| (ii) The Ministry of Environment andForest | - | ||
| (b)Factories other than those mentioned in para. (a) | (i) The Chief Inspector of Factories | The Factories Act, 1948 | |
| (ii) The Inspector of Factories having local jurisdiction | -do- | ||
| (iii) The Ministry of Environment and Forests | - | ||
| 2. | Mine as defined tinder the Mines and Minerals (Regulation and Development) Act. 1957 | (i) [ The Controller-General of Mines] [Substituted by S.O. 64(E), dated 18.1.1988 (w.e.f. 18.1.1988).] | The Mines and Minerals (Regulation and Development) Act, 1957 |
| (ii) Regional Controller of Mines having local jurisdiction] | - | ||
| (iii) The Ministry of Environment and Forests | - | ||
| 3. | Port as defined under the Indian Ports Act, 1908 | (i)Conservator of Ports | The Indian Ports Act, 1908 |
| (ii) The Ministry of Environment and Forests | - | ||
| 4. | Plantationas defined under the Plantations Labour Act, 1951 | (i) The Chief Inspector of Plantations | The Plantations Labour Act, 1951 |
| (ii) The Inspector of Plantations having local jurisdiction | -do- | ||
| (iii) The Ministry of Environment and Forests | - | ||
| 5. | Motor Vehicle as defined under the Motor Vehicles Act, 1939 | (i) State Transport Authority | The Motor Vehicles Act, 1939 |
| (ii) Regional Transport Authority having regional jurisdictions | -do- | ||
| (iii) The Ministry of Environment and Forests | - | ||
| 6. | Ship as defined under the Merchant Shipping Act, 1958 | (i)Director-General of Shipping | The Merchant Shipping Act, 1958 |
| (ii) Surveyor having jurisdiction | -do- | ||
| (iii) The Ministry of Environment and Forests | - |
Part A
Effluents| Sl. No. | Parameter | Standards | |||
| Inland surface water | Public Sewers | Land for irrigation | Marine coastal areas | ||
| 1 | 2 | 3(a) | 3(h) | 3(c) | 3(d) |
| 1. | Colourand odour | See 6 of Annexure I | - | See 6 of Annexure I | See 6 of Annexure 1 |
| 2. | Suspended solids mg/1, Max. | 100 | 600 | 200 | (a) For process waste water-100 |
| (b) For cooling water effluent 10 per cent. above total suspended matter of influent | |||||
| 3. | Particle size of suspended solids | Shall pass 850 micron IS Sieve | - | (a) Floatable solids, Max. 3 mm. | |
| (b) Settleable solids, Max. 850 microns | |||||
| 4. | [***] [Omitted by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | ||||
| 5. | pH value | 5.5-9.0 | 5.5-9.0 | 5.5-9.0 | 5.5-9.0 |
| 6. | Temperature | Shall not exceed 5°C above the receiving water temperature | - | - | Shall not exceed 5°C above the receiving water temperature |
| 7. | Oil and grease mg/1, Max. | 10 | 20 | 10 | [10] [Substituted for the words "20" by Notification No. G.S.R. 739 (E) dated 9.9.2010 (w.e.f. 19.11.1986)] |
| 8. | Total residual chlorine mg/1, Max. | 1.0 | - | - | 1.0 |
| 9. | AmmoniacalNitrogen (as N), mg/1, Max. | 50 | 50 | - | 50 |
| 10. | Total Kjeldahl nitrogen1[N]; mg/1, Max. | 100 | - | - | 100 |
| 11. | Free Ammonia1[NH3]mg/1, Max. | 5.0 | - | - | 5.0 |
| 12. | Biochemical Oxygen demand (5 days at 20°C)1[mg/1, Max] | 30 | 350 | 100 | 100 |
| 13. | Chemical Oxygen demand, mg/1, Max. | 250 | - | - | 250 |
| 14. | Arsenic (as As)1[mg/1], Max. | 0.2 | 0.2 | 0.2 | 0.2 |
| 15. | Mercury (as Hg), mg/1, Max. | 0.01 | 0.01 | - | 0.01 |
| 16. | Lead (as Pb)mg/1, Max. | 0.1 | 1.0 | - | 2.0 |
| 17. | Cadmium (as Cd)mg/1, Max. | 2.0 | 1.0 | - | 2.0 |
| 18. | Hexavalentchromium (as Cr+6) mg/I, Max. | 0.1 | 2.0 | - | 1.0 |
| 19. | Total Chromium (as Cr) mg/1, Max. | 2.0 | 2.0 | - | 2.0 |
| 20. | Copper (as Cu) mg/1, Max. | 3.0 | 3.0 | - | 3.0 |
| 21. | Zinc (as Zn) mg/1, Max. | 5.0 | 15 | - | 15 |
| 22. | Selenium (as Se) mg/1, Max. | 0.05 | 0.05 | - | 0.05 |
| 23. | Nickel (as Ni) mg/1, Max. | 3.0 | 3.0 | 5.0 | |
| [***] [Omitted by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | |||||
| [***] [Omitted by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | |||||
| [***] [Omitted by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | |||||
| 27. | Cyanide (as CN) mg/1, Max. | 0.2 | 2.0 | 0.2 | 0.2 |
| [***] [Omitted by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | |||||
| 29. | [Fluoride] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).](as F) mg/1, Max. | 2.0 | 15 | - | 15 |
| 30. | Dissolved Phosphates (as P) mg/1, Max | 5.0 | - | - | - |
| [***] [Omitted by G.S.R. 801(E), dated 31-12-1993 (w.e.f. 31-12-1993).] | |||||
| 32. | Sulphide(as S) mg/1, Max. | 2.0 | - | - | 5.0 |
| 33. | Phenoliccompounds[as C6H5OH] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]mg/1, Max. | 1.0 | 5.0 | - | 5.0 |
| 34. | Radioactive materials: | ||||
| (a) Alpha emitters1[Micro curie/ml] Max. | 10-7 | 10-7 | 1[10-8] | 10-7 | |
| (b) Beta emitters[Micro curie/ml] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]Max. | 10-6 | 10-6 | 10-7 | 1[10-6] | |
| 35. | Bio-assay test | 90% survival of fish of after 96 hours in 100% effluent | 90% survival of fish of after 96 hours in 100% effluent | 90% survival of fish of after 96 hours in 100% effluent | 90% survival of fish of after 96 hours in 100% effluent |
| 36. | Manganese (as Mn) | 2mg/1 | 2mg/1 | 2mg/1 | |
| 37. | Iron (as Fe) | 3mg/1 | 3mg/1 | 3mg/1 | |
| 38. | Vanadium (as V) | 0.2 mg/1 | 0.2 mg/1 | 0.2 mg/1 | |
| 39. | Nitrate Nitrogen | 10mg/1 | - | - | 20 mg/1 |
| [***] [Entry 40 omitted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] |
Part B
Waste-Water Generation Standards| Sl.No | Industry | Quantum |
| 1. | Integrated IronSteel | 16 [m3/tonne]of finished steel |
| 2. | Sugar | 0.4 [m3/tonne]of cane crushed |
| 3. | Pulp PaperIndustries | |
| (a) Larger pulppaper | ||
| (i) Pulppaper | 175 [m3/tonne]of paper produced | |
| (ii) [ ViscoseStaple Fibre | 150 m3/tonneof product | |
| (iii) ViscoseFilament Yarn | 500 m3/tonneof product] | |
| (b) Small pulppaper: | ||
| (i) Agro-residuebased | 150 [m3/tonne]of paper produced | |
| (ii) Waste paperbased | 50 [m3/tonne]of paper produced | |
| 4. | FermentationIndustries | |
| (a) Maltry | 3.5 [m3/tonne]of grain produced | |
| (b) Brewery | 0.25 [m3/KL]of beer produced | |
| (c) Distillery | 12 [m3/KL]of alcohol produced | |
| 5. | Caustic Soda | |
| (a) Membrane cellprocess | 1 [m3/tonne]of caustic soda produced excluding cooling tower blow down | |
| (b) Mercury cellprocess | 4 [m3/tonne]of caustic soda produced (mercury bearing). | |
| 10% blow downpermitted for cooling tower | ||
| 6. | Textile Industries: | |
| Man-made fibre | ||
| (i) NylonPolyester | 120 [m3/tonne]of fibre produced | |
| (ii) Viscose rayon | 150 [m3/tonne]of product | |
| 7. | Tanneries | 28 [m3/tonne]of raw hide |
| 8. | Starch, Glucoseand related products | 8 [m3/tonne]of maize crushed |
| 9. | Dairy | 3 [m3/KL]of milk |
| 10. | Natural rubberprocessing industry | 4 [m3/tonne]of rubber |
| 11. [ [Substituted by Notification No. G.S.R. 1607(E), dated 29.12.2017 (w.e.f. 19.11.1986).] | Fertiliser Industry | |
| Naphtha, Natural Gas Mixed Feedstock(Naphtha + Natural Gas) Based (Straight Nitrogenous Fertiliser) | 3.0 m3/tonne of Urea or equivalent produced | |
| Straight Phosphatic Fertilizer (Single SuperPhosphate (SSP) Triple Super Phosphate (TSP) excludingmanufacturing of any acid | 0.4 m3/tonne of SSP or TSP | |
| Complex Fertilizer | Standards of nitrogenous and Phosphaticfertiliser are applicable depending on the primary product.] | |
| 12. | Natural RubberProcessing Industry : Centrifuging and Creaming Units and Crapsand Crumb Units- 5 m3/tonne of product in Centrifugingunits;- 8 m3/tonne of product in Creaming units; and- 40m3/tonne of product in Craps and Crumb units. |
Part C
Load Based Standards1. [ Petroleum Oil Refinery :] [Substituted by G.S.R. 186(E), dated 18.3.2008 (w.e.f. 18.3.2008).]
| Parameter | Standard | |
| 1 | 2 | |
| Quantum limit in kg/1,000 tonne of crude processed | ||
| 1. | Oil Grease | 2.0 |
| 2. | BOD days, 27oC | 6.0 |
| 3. | COD3 | 50 |
| 4. | Suspended Solids | 8.0 |
| 5. | Phenols . | 0.14 |
| 6. | Sulphides | 0.2 |
| 7. | CN | 0.08 |
| 8. | Ammonia as N | 6.0 |
| 9. | TKN | 16 |
| 10. | P | 1.2 |
| 11. | Cr (Hexavalent) | 0.04 |
| 12. | Cr (Total) | 0.8 |
| 13. | Pb | 0.04 |
| 14. | Hg | 0.004 |
| 15. | Zn | 2.0 |
| 16. | Ni | 0.4 |
| 17. | Cu | 0.4 |
| 18. | V | 0.8 |
| 19. | Benzene | 0.04 |
| 20. | Benno (α)-Pyrene | 0.08 |
| 2.Large Pulp Paper, News Print/Rayon grade plants of capacity above 24000[tonne] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]/Annum | |
| Parameter | Quantum |
| Total Organic Chloride (TOCI) | 2[kg/tonne] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]of product. |
3. [ Natural Rubber Processing and Rubber Product Industry: Centrifuging and Creaming Units, Craps and Crumb Units.] [Inserted by Notification No. G.S.R. 221 (E) dated 18.3.2011 (w.e.f. 19.11.1986)]
| Parameter | Standards: Quantum limit in kg/100 tonne of finished Products |
| Oil andGrease | 1.5 |
| BOD, 3days at 27°C | 200 |
| SuspendedSolids | 200 |
| TotalChromium | 0.10 |
| Lead | 0.15 |
Part D
General Emission Standards1. Concentration Based Standards:
| Sl. No. | Parameter Concentration not to exceed (in mg/Nm3) | Standard | ||
| 1. | [Particulate Matter (PM) | 150 | ||
| 2. | [Total Fluoride] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | [25] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | ||
| 3. | Asbestos | [4 Fibres/cc and dust should not be more than 2 mg/Nm3] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | ||
| 4. | Mercury | 0.2 | ||
| 5. | Chlorine | 15 | ||
| [6] [Substituted by Notification No. G.S.R. 595 (E), dated 21.8.2009 (w.e.f. 19.11.1986).] | Petroleum Oil refinery (Sulphur Recovery) | Installed Capacity of SRU* (tonne/day) | Kg/tonne of sulphur in the feed to SRU | |
| Existing SRU | New SRU | |||
| Sulphur Dioxide | Above 20 | 26 | 10 | |
| 5 to 20 | 80 | 40 | ||
| Up to 5 | 120 | 80 | ||
| 7 | [***] [Omitted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | |||
| 8. | Sulphuric acid mist | 50 | ||
| 9. | Carbon monoxide | [1% max (v/v)] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | ||
| [***] [Omitted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | ||||
| 11. | Lead | [10 mg/Nm3] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | ||
| [***] [Omitted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] |
| Sl. No. | Parameter | Standard |
| 1. | Sulphurdioxide | Stack-height limit in[metre] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] |
| (i) Power generation capacity: | ||
| -500 MW and more | 275 | |
| -200/210 MW and above to less than 500 MW | 220 | |
| -less than 200/210 MW | H=14 (Q)0.3 | |
| (ii) Steam generation capacity | Coal consumption per day | |
| -Less than 2[tonne/hr] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | [***] [Omitted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | |
| 2 to5 [tonne/hr] | ||
| -5 to 10 [tonne/hr] | ||
| -10 to 15 [tonne/hr] | ||
| -15 to 20 [tonne/hr] | ||
| -20 to 25 [tonne/hr] | ||
| -25 to 30 [tonne/hr] | ||
| -More than 30[tonne/hr] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] |
| Sl.No. | Industry | Parameter | Standard | ||
| 1. | [Fertiliser](Urea) | ||||
| Commissioned priorto 1-1-1982 | [ParticulateMatter (PM)] | 2 [kg/tonne] ofproduct | |||
| Commissioned after1-1-1982 | [ParticulateMatter (PM)] | 0.5 [kg/tonne] ofproduct | |||
| Quantum Limit inkg/tonne Plant capacity for 100% concentration of Sulphuric Acid(tonne/day) | Existing Unit | New Unit | |||
| 2. [] [Substituted by Notification No. G.S.R. 354 (E) dated 2.5.2011 (w.e.f. 19.11.1986)] | Copper, Lead orZinc Smelting Plant | Sulphur-Dioxide(SO2) | Upto 300Above300 | 2.5 | 2.0 |
| 2.0 | 1.5 | ||||
| 3. | Nitric Acid | Oxides of Nitrogen | 3 [kg/tonne] ofweak acid (before concentration) produced | ||
| Quantum Limit inkg/tonne | |||||
| Plant capacity100% | for Existing Unit | New Unit | |||
| Concentration ofSulphuric Acid tonne/day) | |||||
| 4. [] [Substituted by Notification No. G.S.R. 344(E), dated 7.5.2008 (w.e.f. 19.11.1986).] | Sulphuric AcidPlant | Sulphur dioxide(SO2) | Up to 300 | 2.5 | 2.0 |
| Above 300 | 2.0 | 1.5 | |||
| 5. | Integrated Ironand Steel Plant | Carbon monoxideParticulate matterduring coke pushing in coke ovenParticulate matterfor quenching operation in Coke Oven | 3kg/tonne of cokeproduced5 gramme/tonne ofcoke produced50 gramme/tonne ofcoke produced.” | ||
| 6. | Petroleum OilRefinery (Sulphur Recovery) | Installed Capacityof SRU* | Kg/tonne ofsulphur in the feed to SRU | ||
| (tonne/day) | Existing SRU | New SRU | |||
| above 20 | 26 | 10 | |||
| Sulphur Dioxide | 5 to 20 | 80 | 40 | ||
| up to 5 | 120 | 80] | |||
| [***] | |||||
| 7. | Aluminium Plants: | ||||
| (i) Anode BakeOven | Total Fluoride | 0.3 Kg/MT ofAluminium | |||
| (ii) Pot room | |||||
| (a) VSS | -do- | 4.7 Kg/MT ofAluminium | |||
| (b) HSS | -do- | 6 Kg/MT ofAluminium | |||
| (c) PBSW | -do- | 2.5 Kg/MT ofAluminium | |||
| (d) PBCW | -do- | 1.0 Kg/MT ofAluminium | |||
| Note: | |||||
| VSS | = Vertical StudSoderberg | ||||
| HSS | = Horizontal StudSoderberg | ||||
| [PBSW] | = Pre Backed SideWork | ||||
| PBCW | = Pre BackedCentre Work | ||||
| 8. | Glass Industry: | ||||
| (a)FurnaceCapacity | |||||
| (i) Upto theproduct draw capacity of 60 MT/Day | Particulate matter | 2kg/hr | |||
| (ii) Product drawcapacity more than 60 MT/Day | -do- | 0.8 kg/MT ofproduct drawn | |||
| 9. | Petrochemicals(Basic and Intermediates) | Source | Quantumlimit in gm/hour for New/Expansion Plants (gm/hr) | ||
| OrganicParticulate | Phthalic anhydride(PA),Maleic anhydride (MA),Toluene Di-isocyanate (TDI)plants-process emission | 100 | |||
| VOC-HAPs (TDI+MDI) | (TolueneDi-isocyate) TDI, Methylenediphenyl Di-isocynate (MDI)Plants-Process emission | 0.5 | |||
| VOC-HAPs (BenzeneButadiene) | Benzene, ButadienePlants-Process emission | 25.0 | |||
| VOC-HAPs (EO, VCM,EDC, ACN+PO) | EO, VCM, EDC, ACN,PO Plants-Process emission | 50.0 |
Part E
Noise StandardsA. Noise Limits for Automobiles [Free Field Distance at 7.5 Metre] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] in dB(A) at the manufacturing stage| (a) Motorcycles, Scooters Three-wheelers | 80 |
| (b) Passenger Cars | 82 |
| (c) Passenger or Commercial vehicles upto 4 MT | 85 |
| (d) Passenger or Commercial vehicles above 4 MT and upto 12 MT | 89 |
| (e) Passenger or Commercial vehicles exceeding 12 MT | 91 |
| Sl. No. | Type of vehicles | Noise limits dB(A) | Date of implementation |
| 1. | Two wheeler | ||
| Displacement upto 80 cm3 | 75 | ||
| Displacement more than 80 cm3but upto 175 cm3 | 77 | 1st January, 2003 | |
| Displacement more than 175 cm3 | 80 | ||
| 2. | Three wheeler | ||
| Displacement upto 175 cm3 | 77 | ||
| Displacement more than 175 cm3 | 80 | 1st January, 2003 | |
| 3. | Passenger car | 75 | 1st January, 2003 |
| 4. | Passenger or commercial vehicles | ||
| Gross vehicle weight upto 4 tonnes | 80 | ||
| Gross vehicle weight more than 4 tonnes but upto 12 tonnes | 83 | 1st July, 2003 | |
| Gross vehicle weight more than 12 tonnes | 85 |
| Sl. No. | Type of vehicles | Noise limits dB(A) |
| 1.0 | Two wheelers | |
| 1.1 | Displacement upto 80 cc | 75 |
| 1.2 | Displacement more than 80 cc but upto 175 cc | 77 |
| 1.3 | Displacement more than 175 cc | 80 |
| 2.0 | Three wheelers | |
| 2.1 | Displacement upto 175 cc | 77 |
| 2.2 | Displacement more than 175 cc | 80 |
| 3.0 | Vehicles used for the carriage of passengers and capable of having not more than nine seats, including the driver's seat | 74 |
| 4.0 | Vehicles used for the carriage of passengers having more than nine seats, including the driver's seat, and a maximum Gross Vehicle Weight (GVW) of more than 3.5 tonnes | |
| 4.1 | With an engine power less than 150 KW | 78 |
| 4.2 | With an engine power of 150 KW or above | 80 |
| 5.0 | Vehicles used for the carriage of passengers having more than nine seats, including the driver's seat: vehicles used for the carriage of goods | |
| 5.1 | With a maximum GVW not exceeding 2 tonnes | 76 |
| 5.2 | With a maximum GVW greater than 3 tonnes but not exceeding 3.5 tonnes | 77 |
| 6.0 | Vehicles used for the transport of goods with a maximum GVW exceeding 3.5 tonnes | |
| 6.1 | With an engine power less than 75 KW | 77 |
| 6.2 | With an engine power of 75 KW or above but less than 150 KW | 78 |
| 6.3 | With an engine power of 150 KW or above: | 80 |
| (a) | Window Air Conditioners of 1 tonnes to 1.5 tonnes | 68 |
| (b) | Air[coolers] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] | 60 |
| (c) | Refrigerators | 46 |
| [***] [Entry (d) omitted by G.S.R. 371(E), dated 17.5.2002 (w.e.f. 17.5.2002).] | ||
| (e) | compactors(rollers), Front loaders, Concrete mixers, Cranes (movable), Vibrators and Saws. | 75 |
1. The waste-waters and gases are to be treated with the best available technology [(BAT)] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] in order to achieve the prescribed standards.
2. The industries need to be encouraged for recycling and reuse of waste materials as far as practicable in order to minimise the discharge of wastes into the environment.
3. The industries are to be encouraged for recovery of biogas, energy and reusable materials.
4. While permitting the discharge of effluents and omissions into the environment, State Boards have to take into account the assimilative capacities of the receiving bodies, especially water bodies so that quality of the intended use of the receiving water is not affected. Where such quality is likely to be affected, discharges should not be allowed into water bodies.
5. The Central and State Boards shall put emphasis on the implementation of clean technologies by the industries in order to increase fuel efficiency and reduce the generation of environmental pollutants.
6. All efforts should be made to remove colour and unpleasant odour as far as practicable.
7. The standards mentioned in this Schedule [shall also apply to all other effluents] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] discharged such as mining, and mineral processing activities and sewage.
8. The limit given for the total concentration of mercury in the final effluent of caustic soda industry, is for the combined effluent from (a) Cell house, (b) Brine plant, (c) Chlorine handling, (d) Hydrogen handling, and (e) Hydro chlorie acid plant.
[***] [Clause (9) omitted by G.S.R. 176(E), dated 2.4.1996 (w.e.f. 3.4.1996).]10. All effluents discharged including from the industries such as cotton textile, composite woollen mills, synthetic rubber, small pulp and paper, natural rubber, petro-chemicals, tanneries, paint, dyes, slaughter houses, food fruit processing and dairy [industries] into surface waters shall conform to the BOD limits specified above, namely, 30 mg/ 1. For discharge of an effluent having a BOD more than 30 mg/1, the standards shall conform to those given above for other receiving bodies, namely, sewers, coastal waters and land for irrigation.
[***] [Clause (11) omitted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]12. In case of fertilizer industry the limits in respect of chromium and [fluoride] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] shall be complied with at the outlet of chromium and [fluoride] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).] removal units respectively.
13. In case of pesticides :
14. [ The chemical oxygen demand (COD) concentration in a treated effluent, if observed to be persistently greater than 250 mg/1 before disposal to any receiving body (public sewer, land for irrigation, inland surface water and marine coastal areas), such industrial units are required to identify chemicals causing the same. In case these are found to be toxic as defined in the Schedule I of the Hazardous Wastes (Management and Handling) Rules, 1989 the State Boards in such cases shall direct the industries to install tertiary treatment stipulating time limit.
15. Standards specified in Part A of Schedule VI for discharge of effluents into the public sewer shall be applicable only if such sewer lead to a secondary treatment including biological treatment system, otherwise these discharge into sewers shall be treated as discharge into inland surface waters.] [Inserted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]
ANNEXURE II(For the purpose of Part D)1. The State Boards shall follow the following guidelines in enforcing the standards specified under Schedule VI:
2. The total fluoride emissions in respect of Glass and Phosphatic Fertilizers shall not exceed 5 mg/NM³ and 25 mg/NM³ respectively.
3. [In case of copper, lead and zinc smelting, the off-gases may, as far as possible, be utilised for manufacturing sulphuric acid.] [Substituted by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]
4. [ In case of cupolas (Foundries) having capacity (melting rate) less than 3 tonne/hour, the particulate matter emission shall be within 450 mg/Nm³. In these cases it is essential that stack is constructed over the cupola beyond the charging door and the emissions are directed through the stack, which should be at least six times the diameter of cupola. In respect of Arc Furnaces and Induction Furnaces, provision has to be made for collecting the fumes before discharging the emissions through the stack.] [Added by G.S.R. 801(E), dated 31.12.1993 (w.e.f. 31.12.1993).]
[SCHEDULE VII [Substituted by Notification No. G.S.R. 826 (E) dated 16.11.2009 (w.e.f. 19.11.1986)][See rule 3(3-B)]NATIONAL AMBIENT AIR QUALITY STANDARDS| S.No. | Pollutant | Time Weighted Average | Concentration in Ambient Air | ||
| Industrial, Residential, Rural and Other Area | Ecologically Sensitive Area (notified byCentral Government) | Methods of Measurement | |||
| (1) | (2) | (3) | (4) | (5) | (6) |
| 1 | Sulphur Dioxide (SO2), µg/m3 | Annual*24 hours** | 5080 | 2080 | - Improved West and Gaeke- Ultraviolet fluorescence |
| 2 | Nitrogen Dioxide (NO2), µg/m3 | Annual*24 hours** | 4080 | 3080 | - Modified Jacob Hochheiser (Na-Arsenite)-Ultraviolet fluorescence |
| 3 | Particulate Matter (size less than 10µm) or PM10µg/m3 | Annual*24 hours** | 60100 | 60100 | - Gravimetric- TOEM- Beta attenuation |
| 4 | Particulate Matter (size less than 2.5µm) or PM2.5µg/m3 | Annual*24 hours** | 4060 | 4060 | - Gravimetric- TOEM- Beta attenuation |
| 5 | Ozone(O3) µg/m3 | 8 hours**1 hour** | 100180 | 100180 | - UV photometric- Chemi Iminescence- Chemical Method |
| 6 | Lead(Pb) µg/m3 | Annual*24 hour** | 0.501.0 | 0.501.0 | - AAS/ICP method after sampling on EPM 2000 or equivalentfilter paper- ED-XRF using Teflon filter |
| 7 | Carbon Monoxide (CO) mg/m3 | 8 hours1 hour | 0204 | 0204 | - Non Dispersive Infra Red (NDIR) spectroscopy |
| 8 | Ammonia(NH3)µg/m3 | Annual*24 hours** | 100400 | 100400 | - Chemiluminescence- Indophenol blue method |
| 9 | Benzene(C6H6) µg/m3 | Annual* | 05 | 05 | - Gas chromatography based continuous analyzer- Adsorptionand Desorption followed by GC analysis |
| 10 | Benzo(α) Pyrene (BaP) - particulate phase only, ng/m3 | Annual* | 01 | 01 | - Solvent extraction followed by HPLC/GC analysis |
| 11 | Arsenic(As), ng/m3 | Annual* | 06 | 06 | - AAS/ICP method after sampling on EPM 2000 or equivalentfilter paper |
| 12 | Nickel (Ni), ng/m3 | Annual* | 20 | 20 | - AAS/ICP method after sampling on EPM 2000 or equivalentfilter paper |
| [SCHEDULE VII] [Inserted by G.S.R. 176(E), dated 2.4.1996 (w.e.f. 3.4.1996).][See rule 3(3-B)]NATIONAL AMBIENT AIR QUALITY STANDARDS (NAAQS){| | |||||
| Pollutant | Time Weighted Average | Concentration in Ambient Air | |||
| Industrial Area | Residential, Rural and Other Area | Sensitive Area | Method of Measurement | ||
| (1) | (2) | (3) | (4) | (5) | (6) |
| SulphurDioxide | Annual Average* | 80µg/m3 | 60µg/m3 | 15µg/m3 | - Improved West and Greke method |
| (SO)2 | 24hours** | 120µg/m3 | 80µg/m3 | 30µg/m3 | - Ultraviolet Fluorescence |
| Oxides of nitrogen as No2 | Annual Average | 80µg/m3 | 60µg/m3 | 15µg/m3 | - Jacab and Hochheiser modified (Na-Arsenite) Method |
| 24hours** | 120µg/m3 | 80µg/m3 | 30µg/m3 | - Gas Phase Chemiluminescence | |
| Suspended Particulate Matter (SPM) | Annual Average* | 360µg/m3 | 140µg/m3 | 70µg/m3 | - High Volume Sampling |
| 24hours** | 500µg/m3 | 200µg/m3 | 100µg/m3 | - [Average flow rate not less than1.1m3/minute] | |
| RespirableParticulate Matter (size less than 10 um) (RPM) | Annual Average* | 120µg/m3 | 60µg/m3 | 50µg/m3 | - Respirable Particulate matter sampler. |
| 24hours** | 150µg/m3 | 100µg/m3 | 75µg/m3 | ||
| Lead (Pb) | Annual Average* | 1.0µg/m3 | 0.75µg/m3 | 0.50gg/m3 | - AAS method after sampling using |
| 24hours** | 1.5µg/m3 | 1.00g/m3 | 0.75µg /m3 | EMP 2000 or equivalent filter paper. | |
| Carbon | 8hours** | 5.0mg/m3 | 2.0mg/m3 | 1.0mg/m3 | - Non-dispersive, infrared spectroscopy. |
| Monoxide | 1hour | 10.0mg/m3 | 4.0mg/m3 | 2.0mg/m3 |
2. Whenever and wherever two consecutive values exceeds the limit specified above for the respective category, it shall be considered adequate reason to institute regular/continuous monitoring and further investigations.
|}APPENDIX AFORM I(See rule 7)NOTICE OF INTENTION TO HAVE SAMPLE ANALYSEDTo........................................................................Take notice that it is intended to have analysed the sample of* ............................which has been taken today, the ..........................................day of............................... 20...................... from* ............................................................. (Name and designation of the person who takes the sample).(Seal)Date ....................................*Specify the place from where the sample is taken.FORM II(See rule 8)MEMORANDUM TO GOVERNMENT ANALYSTFrom....................................................ToThe Government Analyst...............................................................................................................The portion of sample described below is sent herewith for analysis under rule 6 of the Environment (Protection) Rules, 1986.The portion of the sample has been marked by me with the following mark:Details of the portion of samples taken.Name and designation of person who sends the sample(SEAL)Date ................................FORM III(See rule 8)REPORT BY GOVERNMENT ANALYSTReport No. ...............................Date .........................................I hereby certify that I ..........................................Government Analyst duly appointed under section 13 of the Environment (Protection) Act, 1986 received on the .......................................day of ........................... 20............................................. from ......................................................*.........................................................................a sample of .............................................for analysis.The sample was in a condition fit for analysis as reported below.I further certify that I have analysed the aforementioned sample on ..........................and declare that the result of the analysis to be as follows:**......................................................................................................................................................................................................................................The condition of seals, fastening of samples on receipt was as follows:Signed this ......................................................................day of.............................................................................20........................................................Address ...........................................................Signature(Government Analyst)To.................................................................................................................................*Here write the names of the officer/authority from whom sample was obtained.**Here write full details of analysis and method of analysis.FORM IV(See rule 11)FORM OF NOTICEBy registered post-acknowledgment dueFrom (1)Shri.................................................................................................................To................................................................................Notice under section 19(b) of the Environment (Protection) Act, 1986Whereas an offence under the Environment (Protection) Act, 1986 (29 of 1986) has been committed/is being committed by ............................(2) I/We hereby give notice of 60 days under section 19(b) of Environment (Protection) Act, 1986 (29 of 1986) of my/our intention to file a complaint in the Court against ..............................(3) for violation of section........................of the Environment (Protection) Act, 1986 (29 of 1986).In support of my/our notice, I am/we are enclosing the following documents (3) as evidence of proof of violation of the Environment (Protection) Act, 1986 (29 of 1986).Place ....................................Date ........................................................................Signature(s)Explanation. - (1) In case the notice is given in the name of a company, documentary evidence authorising the person to sign the notice on behalf of the company shall be enclosed to this notice.Company for this purpose means a company defined in the Explanation to sub-rule (6) of rule 4.Part A
Part B
Water and Raw Material Consumption| Name of products | Process water consumption per unit of product output | |
| During the previous financial year | During the current financial year | |
| (1) | ||
| (2) | ||
| (3) |
| *Name of raw materials | Name of products | Consumption of raw material per unit of output | |
| During the previous financial year | During the current financial year |
Part C
Pollution discharged to environment/unit of output(Parameter as specified in the consent issued)| Pollutants | Quantity of pollutants discharged (mass/day) | Concentrations ofpollutants in discharges (mass/volume) | Percentage of variation from prescribed standards with reasons |
| (a) Water | |||
| (b) Air |
Part D
Hazardous Wastes(As specified under Hazardous Wastes (Management and Handling) Rules, 1989)| Hazardous Wastes | Total Quantity (Kg) | |
| During the previous financial year | During the current financial year | |
| (a) From process | ||
| (b) From pollution control facilities. |
Part E
Solid Wastes| Total Quantity (Kg) | ||
| During the previous financial year | During the current financial year | |
| (a) From process | ||
| (b) From pollution control facility | ||
| (c) (1) Quantity recycled or re-utilised within the unit | ||
| (2) Sold | ||
| (3) Disposed |