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[Cites 8, Cited by 0]

Delhi High Court

Lummus Novolen Technology Gmbh vs The Assistant Controller Of Patents And ... on 29 May, 2025

                          *          I N T H E H I G H CO U R T O F D E L H I A T N E W D E L H I

                                                                                Reserved on: April 24, 2025
                          %                                                   Pronounced on: May 29, 2025

                          +                            C.A.(COMM.IPD-PAT) 12/2023
                                     LUMMUS NOVOLEN TECHNOLOGY GMBH           .....Appellant
                                                Through: Ms. Vindhya S. Mani, Ms. Naina
                                                         Gupta, Mr. Bhuvan Malhotra, Ms.
                                                         Vedika Singhvi, Mr. Ritwik Sharma,
                                                         Ms. Surbhi Nautiyal, Mr. Devesh
                                                         Aswal and Ms. Narshita Agarwal,
                                                         Advs.

                                                                     Versus

                              THE ASSISTANT CONTROLLER OF PATENTS AND
                              DESIGNS                                   .....Respondent
                                            Through: Ms. Nidhi Raman, CGSC with Mr.
                                                     Arnav Mittal, Adv.
                          CORAM:
                          HON'BLE MR. JUSTICE SAURABH BANERJEE
                                                                JUDGMENT

Preface:

1. Vide the present appeal under Section 117A of the Patents Act, 19701 the appellant seeks to assail the order dated 30.01.2023 passed by the Assistant Controller of Patents and Designs2, who has rejected its Indian 1 Hereinafter referred as "1970 Act"
2
Hereinafter referred as "Controller"
C.A.(COMM.IPD-PAT) 12/2023 Page 1 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06

Patent Application No.4278/DELNP/2015 dated 19.05.20153 under Section 15 of the 1970 Act since "...The subject matter of claims 1-9 is not allowed u/s 2(1)(ja) as it does not involve any inventive step and is obvious in view of the combined teachings of cited documents D1 to D3. ...". As such, in effect the subject application has been rejected on the ground that it involves no "inventive step" under Section 2(1)(ja)4 of the 1970 Act.

2. Therefore, the short question for determination before this Court is "Whether any "inventive step" under Section 2(1)(ja) of the 1970 Act are involved in Claim no.1 to 9 of the subject application filed by the appellant?".

Brief narrative facts:

3. The appellant, Lummus Novolen Technology Gmbh, is a global provider of process technologies and value-driven energy solutions, including performance polypropylene (PP) polymers, a family of products that have the properties of recycled polymers and is a company incorporated under the laws of Germany and has its registered office at Gottlieb Daimler Str. 8 68165, Mannheim, Germany.

4. The appellant filed the subject application with title "HIGH PERFORMANCE ZIEFLERNATTA CATALYST SYSTEMS, PROCESS FOR PRODUCING SUCH MgC12 BASED CATALYSTS AND USE THEREOF"

3
Hereinafter referred as "subject application"
4

Section 2(ja) "inventive step" means a feature of an invention that involves technical advance as compared to the existing knowledge or having economic significance or both and that makes the invention not obvious to a person skilled in the art.

C.A.(COMM.IPD-PAT) 12/2023 Page 2 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06

before the Patent Office, New Delhi5 on 19.05.2015, whereafter the request for examination thereof was filed on 19.05.2015, and the same was then published in the Patent Journal on 22.07.2016.

5. In the First Examination Report6 issued by the Patent Office on 12.02.2019, majorly the following issues were raised:-

"- Subject matter of claims 1-13 lacks novelty under Section 2(1)(i) of the Act in view of the documents:
i. D1: EP 1840138 Al; annexed herewith as Document 5. ii. D2: EP 1609805 Al; annexed herewith as Document 6. iii. D3: WO 2009152268 Al; annexed herewith as Document 7.
- Subject matter of claims 1 to 13 lacks inventive step under Section 2(1)(ja) of the Act in view of the documents;
                                       i.    D1: EP 1840138 A1
                                       ii.   D2: EP 1609805 Al
                                       iii. D3: WO 2009152268 Al

                                       -      The abstracts, title and drawings do not meet the criteria of
sufficiency of disclosure under Section 10(4) of the Act read with Rule 13(7) and Rule 15 of the Patent Rules, 2003.
- Subject matter of claims 1-13 do not meet the requirements of
- definitiveness under Section 10(4)(c) of the Act.
- Subject matter of claims 2-13 are inconsistent and beyond the scope of claim 1."

6. In response thereto, on 10.05.2019, the appellant also filed its amended claims before the Patent Office, whereafter, a Hearing Notice dated 23.02.2021 was issued by the Controller for 27.04.2021, however, since the appellant filed a request for adjournment, though the Controller issued an extended Hearing Notice for 13.08.2021 but raised the following substantive objections under Section 14 of the 1970 Act:-

5
Hereinafter referred as "Patent Office"
6
Hereinafter referred as "FER"
C.A.(COMM.IPD-PAT) 12/2023 Page 3 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06
"- The subject matter as claimed in claims 1-10 of the alleged invention is not patentable under Section 2(1)(ja) in view of the further cited documents;
                                     i.     Dl: EP 1840138 Al
                                     ii.    D2: EP 1609805 Al
                                     iii. D3: WO 2009152268 Al

                                     -     The subject matter of the claims in the Indian Patent Application
No. 4278/DELNP/2015 conflicts with the subject matter of the claims in Indian Patent Application No. 4277/DELNP/2015.
- The subject matter of claims 2-10 are inconsistent and beyond the scope of claim 1."

7. After attending the hearing, the appellant filed a written submission on 08.10.2021 wherein, it amended and deleted Claims 1 and 10, leaving amended Claims 1 to 9, whereafter, the Controller passed the impugned order on 30.01.2023, refusing to grant the Patent application.

8. Aggrieved thereby, the appellant has preferred the present appeal. Contentions of learned counsel for Appellant:

9. Ms. Vindhya S. Mani, learned counsel for the appellant raised the following contentions:-

9.1. Since the impugned order is silent about or has any proper reasoning therein, as to why arguments in the written submissions were not found convincing to the respondent which violates the principles of natural justice.

For this, reliance was placed upon Wisig Networks Private Limited vs. Controller General of Patents, Design, Trademark & Geographical Indications7; Assistant Commissioner Kota vs. Shukla & Bros8; and Kranti 7 2020 SCC OnLine IPAB 198 8 (2010) 4 SCC 785 C.A.(COMM.IPD-PAT) 12/2023 Page 4 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 Associates Private Limited & Anr. vs. Masood Ahmed Khan & Ors.9. 9.2. The Controller has not considered the technical advancement offered by the claimed invention i.e., new process for producing a Ziegler-Natta catalyst having improved activity of olefin polymerization essentially from non-phthalate polymers and the activity of the catalyst leading to higher product yields and reducing the quantity of the catalyst for olefin polymerization reaction which in turn reduces the catalyst cost and the amount of catalyst impurities in the polymers (reduced ash content), resulting in polymers with better performance profile and the invention in the present patent application relates to an Ziegler-Natta catalyst, particularly an improved method for making a Ziegler-Natta catalyst essentially using diether compounds as internal donor.

9.3. The Controller has merely reproduced the paragraphs in the impugned order from the decision of the European Patents Office dated 16.03.2021 in the corresponding European Application No.13802264.5, which is contrary to the settled position of law, particularly, since the patent jurisprudence is territorial in nature and each patent application has to considered on its own merits within every jurisdiction and not use 'cut and paste' methodology. For this, reliance was placed upon R.C. Sharma vs. Union of India & Ors.10; Dolby International Ab vs. The Assistant Controller of Patents & Designs11. 9.4. Similar claims have been granted in other jurisdictions inter alia United States of America, China, Japan, Republic of Korea and Israel which 9 (2010) 9 SCC 496 10 (1976) 3 SCC 574 11 2023:DHC:1854 C.A.(COMM.IPD-PAT) 12/2023 Page 5 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 clearly indicates inventive merit, patentability, commercial interest and industrial applicability of claimed invention. For this, reliance was placed upon Stempeutics Research Pvt. Ltd. vs. Assistant Controller of Patent & Designs 202012.

9.5. The refusal of grant of patent by the Controller on the ground of lack of inventive step of the pending amended claim in view of the cited prior art documents D1 to D3 hold no merit for the reason that none of the references, collectively or individually, teach or suggest the claimed invention, or direct modifications of prior art documents to arrive at the present invention. 9.6. The Controller has wrongly placed reliance on Examples 13 and 15 of the cited prior art document D1 relating to the catalyst allowing the preparation of polypropylene with a molecular weight distribution of 7 and document D1 in Examples 13 and 15 which teaches about the use of phthalate based cyclic ester compound to produce desirable polymer i.e., diethyl-cyclohex-4-ene-1,2-dicarboxylate i.e., diethyl 1,2,3,6- tetrahydrophthalate and diisobutyl cyclohexane-1,2-dicarboxylate also known as diisobutyl hexahydrophthalate. This is, since the invention in the present matter exclusively involves non-phthalate-based catalysts for production of polymers and phthalate-based compounds pose health and environmental challenges, whereas, phthalate free polymers eliminates the safety concerns regarding health and environment, particularly related to packaging food and health products, therefore, the cited prior art document D1 is an unrelated 12 SCC OnLine IPAB 16 C.A.(COMM.IPD-PAT) 12/2023 Page 6 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 prior art document and does not teach or suggest about Ziegler-Natta catalyst system comprising a diether compound as the only internal electron donor. 9.7. The Controller has incorrectly found Examples 8, 10 and 14 of the cited prior art document D2 which disclose polypropylenes having molecular weight distribution of 7 or 7.1 which is included in the range of 5.75 to 9, however, the claimed process pertains to "a spherical spray-cooled MgCl2- xROH 1.5 to 6". The cited prior art document D2 is directed to a composite carrier of catalysts for olefin polymerization, particularly, since it teaches about a composite carrier of catalysts for propylene polymerization comprising magnesium halide and silica material with an average particle size of less than 10 microns. On the contrary, such composite carrier is excluded by the carrier recited in Claim 1 of the subject invention and "... ...if a catalyst is prepared by employing I ,3-diether compounds as internal electron donor yet no composite carrier according to the present invention, the obtained polymer has a narrower molecular weight distribution as shown in Comparative Example... ...". More so, cited prior art document D2 does not teach about the use of 1,3-diether compounds as the internal electron donor while obtaining an activity and hydrogen response suitable for the production of propylene polymers having a molecular weight distribution (PI(GPC)) in the range from about 5.75 to about 9.

9.8. The cited prior art document D3 fails to teach about broader molecular weight distribution i.e., greater than 5.75 as desired by the present invention and a person skilled in the art from teachings thereof would be prompted to use phthalates such as dialkylphthalates like diaisobutylphthalate (D-i-BP) or C.A.(COMM.IPD-PAT) 12/2023 Page 7 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 di-n-butylphthalate (D-n-BP) as preferred internal donors over diethers, and/ or the electron donors of the cited prior art document D3 in combination with the cyclic ester of other disclosures. Thus, the cited prior art document teaches away from the claimed invention and further, it is important to note that document D3 fails to recognize the differences in phthalate and diethers as internal electron donors, and the use of the claimed diethers resulting in unexpectedly claimed advancements. Hence, document D3 fails to teach, suggest, or motivate a person skilled in the art use of diethers to make a Ziegler-Natta catalyst for the polymerization of olefins, wherein the catalyst has unusually high activity, excellent hydrogen response and stereoselectivity while the molecular weight distribution is comparable to phthalate containing Ziegler-Natta catalysts.

9.9. The impugned order is bereft of any basis/ assertion/ reasoning viz. why a person skilled in the art would read the prior art documents together or that why such a person skilled in the art after reading the closest prior art document D1 would be motivated to read the cited prior art documents D2 and D3 for arriving at the claimed invention. More so, there is no reasoning qua linking the cited prior art documents D1, D2 and D3 together. 9.10. The Controller has not taken into consideration the settled judicial precedents for raising the ground of lack of inventive step, and has combined the cited prior art documents D1, D2 and D3 together in mere hindsight, and that too despite lack of motivation available to a person skilled in the art which is not permissible under the law. For this, reliance was placed upon F. C.A.(COMM.IPD-PAT) 12/2023 Page 8 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 Hoffmann-La Roche Ltd. & Anr. vs. Cipla Ltd.13; Bristol-Myers Squibb Holdings Ireland Unlimited Company & Ors. vs. BDR Pharmaceuticals International Pvt. Ltd. & Ors.14; Prism Cement Ltd. vs. The Controller of Patents & Designs15.

9.11. The prior art taught the use of a laminate comprising of a PVA film in combination with a non-woven fabric. Reliance was placed on the judgement of the Madras High Court in Kuraray Co. Ltd. vs. Assistant Controller of Patents & Designs16, wherein the court was of the view that a person skilled in such prior art would not be motivated to consider the use of a PVA film on a standalone basis for resolving the problem that the claimed invention intended to resolve.

9.12. Lastly, in Novozymes vs. Assistant. Controller of Patents17 while dealing with two cited prior art documents D8 and D9 therein, the High Court of Madras held that the prior art document D9 solves a different problem then the claimed invention and that the cited prior art document D8 was closer to the claimed invention but that too would not be able to make the claimed invention obvious to the person skilled in the art. Contentions of the CGSC for Controller:

10. Per contra, Ms. Nidhi Raman, learned Central Government Standing Counsel for the respondent Controller raised the following contentions:-

10.1. The appellant herein had simultaneously filed two almost similar 13 2015:DHC:9674-DB 14 2020 SCC OnLine Del 1700 15 2020 SCC OnLine IPAB 25 16 2023 SCC OnLine Mad 7568 17 2024:MHC:1344 C.A.(COMM.IPD-PAT) 12/2023 Page 9 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 patent application nos. 4277/DELNP/2015 and 4278/DELNP/2015 before the Indian Patents Office on 19.05.2015. Both were heard separately on 15.09.2021 itself by the same Controller, who after detailed examination, allowed the patent application no. 4277/DELNP/2015 pertaining to a process for manufacturing a Ziegler-Natta catalyst with a specific activity and hydrogen response leading to the production of propylene polymers within a defined molecular weight distribution range (PI(GPC)) of 5.75 to 9 on 31.01.2022 but dismissed the other patent application no. 4278/DELNP/2015 on the grounds that the invention therein was deemed exceedingly apparent in light of the cited prior art documents D1, D2 and D3, which is under challenge herein.
10.2. The above said patent application no. 4277/DELNP/2015 claimed two similar distinguishing features (i) in relation to step (e) of the process, which involves filtering the reaction mixture while it was still in a heated state; and
(ii) using a 1, 3-diether compound as an internal electron donor and the applicant's submission for Claim 9, made subsequent to the hearing, clearly indicates that both the Ziegler-Natta catalysts described in said applications exhibited similar levels of activity and hydrogen response. In the impugned order, the Controller has extracted specific passages from the cited prior art documents D1, D2 and D3 in order to illustrate the similarities between the present patent application and the disclosures contained in the cited prior art documents D1, D2 and D3 and there was apparent overlap which was coincidental and not indicative of any improper influence. Moreover, the cited prior art document D1 is considers as a closest prior art, as it C.A.(COMM.IPD-PAT) 12/2023 Page 10 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 demonstrates a catalyst preparation process akin to the present patent application. Also, Example 13 of the cited prior art document D1 demonstrates the preparation of polypropylene with a molecular weight distribution falling within the range targeted by the present patent application (5.75 to 9) and it employs a catalyst preparation process that shares similarities with the present patent application, including the use of the same internal electron donor, 2-isobutyl-2-isopropyl-1, 3-dimethoxypropane, and involved a step of hot filtration. As such, the specifics of Example 13 of the cited prior art document D1 are elucidated in the inventive step section.

10.3. The cited prior art document D2 also offers processes for the preparation of Ziegler-Natta catalyst yielding polypropylene with a similar molecular weight distribution and the disclosed processes in Examples 8, 10, and 14 of the cited prior art document D2 exhibit the production of polypropylenes with a molecular weight distribution of 7 or 7.1, which fell within the targeted range of 5.75 to 9, which is similar to what is described in the present patent application. As such, the specifics of Examples 8, 10, and 14 of the cited prior art document D2 are elucidated in the inventive step section.

10.4. The cited prior art document D3, which was originating from the same applicant as the present invention, describes a process exactly identical to the one claimed in the present patent application (Claim 1 and paragraphs [0018]- [0028]), albeit with only a minor distinction in the broader definition of the electron donor, as found in Claims l, 15 of the cited prior art document D3. Also, paragraph [0040] of the cited prior art document D3 suggests the C.A.(COMM.IPD-PAT) 12/2023 Page 11 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 use of non-substituted and substituted (CL-CLO alkyl)-1,3-propane diethers and derivatives of succinates as internal electron donors. The cited prior art document D3 also specifies a spherical MgCl2-xROH support, ideally characterized by a d50 particle size ranging from 40 to 90 microns, which can be produced through the spray-cooling method. Similarly, paragraph [0061] of the same cited prior art document D1 mentions the use of a sixty-micron (d50) MgCl2.3.2EtOH support, which is similar to that used in the examples of the present patent application. As such, a skilled person in the field would employ such a support in the process described in Example 13 of the cited prior art document D1, incorporating an extraction step as disclosed in the general process of the cited prior art document D3. The expected result would thus be a process in alignment with the claims outlined in the present invention (Claim 1).

10.5. The cited prior art document D1 involves the use of both ethers and diethers, however, it indicated that either of these compounds can be employed. In fact, paragraphs [0072] & [0079] of the cited prior art document D1 suggest the use of certain diethers in combination with the solid titanium catalyst component. The cited prior art document D1 also establishes that the use of similar l,3-diether compounds can lead to the production of polypropylene (pp) with an MWD (GPC) of 7 and the recovery of a solid portion via hot filtration, emphasizing that this information is not limited to the specific compounds mentioned in the examples. 10.6. The appellant emphasizes the use of diethers in combination with silica in the cited prior art document D2, however, similar l,3-diether compounds C.A.(COMM.IPD-PAT) 12/2023 Page 12 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 can be used in Ziegler Natta catalysts to achieve a polypropylene (pp) with an MWD (GPC) of 7.1, as demonstrated in D2 and the present invention also utilizes silica inherently present in the MgCl2-xRoH support, as evident from the subject matter of Claim 1 which claimed a similar Ziegler-Natta catalyst with silica as the carrier. Though this was initially filed with the FER response of the present patent application but was later deleted by the appellant due to conflicts with the already granted application 4277/DELNP/2015. In any event, the appellant never provided any studies demonstrating that the properties of the catalyst, including its activity and hydrogen response, resulting in the production of propylene polymers with a specific molecular weight distribution (PI(GPC)), which are solely attributed to the use of diether compounds as internal electron donors. The already granted patent application no. 4277/DELNP/20l5, featuring a similar Ziegler- Natta catalyst with silica as the carrier and employing similar 1,3-diether compounds as internal donors, yields the same results regarding catalyst properties and polypropylene production.

10.7. Lastly, both cited prior art documents D1 and D2 are identified as the most relevant for the present invention due to their disclosure of using an internal electron donor composed mainly of a diether compound and filtering the pre-catalyst mixture while it is still hot. The cited prior art document D3, while using phthalate compounds as internal donors, outlines a process that aligns closely with the parameters of the cited prior art documents D1 and D2 as the resulting solid catalyst component therein demonstrates activity and hydrogen response suitable for producing propylene polymers with a C.A.(COMM.IPD-PAT) 12/2023 Page 13 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 molecular weight distribution similar to the present invention. Consequently, the present invention emerges as a predictable outcome when the process steps and parameters of the cited prior art document D3 are combined with the disclosures of the cited prior art documents D1 and D2 which utilize a diether compound as an internal electron donor and hot filtration. In essence, the present invention lacks inventive step when considering the amalgamation of cited prior art document D3 with the teachings of the cited prior art documents D1 and D2. Therefore, the inventive step is analysed in comparison with the cited prior art document D3.

Discussion, analysis and reasonings:

11. This Court has heard both Ms. Vindhya S. Mani, learned counsel for the appellant and Ms. Nidhi Raman, learned Central Government Standing Counsel for the respondent, as also perused the documents on record and taken note of the judgments cited by them as well.

12. Before proceeding, the abstract from the present patent application is reproduced as under:-

C.A.(COMM.IPD-PAT) 12/2023 Page 14 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06

13. From the above abstract, it is borne out that the subject application entails an improved Zeigler-Natta catalyst and method of making the improved catalyst. However, the same is sufficient for grant of a patent has to be seen taking into account the relevant provisions of Section 2(1)(ja) of the 1970 Act.

14. Section 2(1)(j)18 of the 1970 Act reveals that grant of a patent of an 'invention' is dependent upon three factors, namely, the patent has to be a 'new product or process' involving an 'inventive step' and having an 'industrial application'.

15. Similarly, the said 'inventive step' under Section 2(1)(ja) of the 1970 Act must involve 'technical advance as compared to the existing knowledge' either having an 'economic significance' or both 'technical advance as compared to the existing knowledge' and 'economic significance', and furthermore the said invention should not be 'obvious to a person skilled in the art'.

16. In the present case, the Controller has refused the grant of the patent application of the appellant since the invention in subject application did not have an inventive step as defined under of Section 2(1)(ja) of the 1970 Act. As such the invention did not involve an 'inventive step' as the Claim(s) made therein were 'obvious to a person skilled in the art'.

17. Therefore, while dealing with Section 2(1)(ja) of the 1970 Act, the prime factors for an 'inventive step', is that there has to be some 'technical 18 2(1)(j)"invention" means a new product or process involving an inventive step and capable of industrial application;

C.A.(COMM.IPD-PAT) 12/2023 Page 15 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06

advance as compared to the existing knowledge' and which is not to be (vi) obvious to a person skilled in the art'. As such, an invention in a patent application has to have a technical advancement from the existing information available to the public at large in the form of prior art(s); and the embodiments in the Claim(s) made therein when seen from the eyes of a person skilled in the art must not be obvious, so that a person skilled in the art comes to the same invention, so that the monopoly granted to a patentee is justified by the patentee's contribution in the art for the term of the patent.

18. Therefore, all Claim(s) in a patent application like the present one before the Controller have to be evaluated upon considering the cited prior art documents therein, with a view to verify, if the invention so claimed does indeed involves a major technical advancement(s) and not minor changes/ variations. This is particularly to augment but not hamper, and vice versa, the natural development(s)/ advancement(s) in an Industry without monopolising the patent in favour of the patentee and recognising the contribution of an inventor in the art by balancing the good of the public and/ or of the said industry.

19. Oner time, various test(s), like those hereunder, have evolved for judging the scales of 'obviousness' and 'lack of inventive step':-

i. Obvious to try approach is to identify if a patentee has chosen from a finite number of identified, predictable solutions with a reasonable expectation of success as such the invention becomes obvious; and ii. Problem/ solution approach to proceed for initially identifying C.A.(COMM.IPD-PAT) 12/2023 Page 16 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 a problem in the Claim(s) made, and then finding a solution thereto to ascertain if the solution are/ can be known to a person skilled in the art in the concerned field; and iii. Could-Would approach to proceed to determine if an invention is obvious to a person skilled in the art. It involves asking whether, based on the existing prior art, a skilled person would have arrived at the claimed invention than could. In essence, it focuses on identifying a motivation or prompting in the prior art that would lead a skilled person to make the invention.
iv. Teaching Suggestion Motivation (TSM test) to identify if any ordinary person skilled in the art in the concerned can modify the prior art to arrive at the claimed invention, if so, then subject matter claimed is obvious.

20. For better understanding the scope of invention in the patent application i.e., the amended Claim 1 thereof for producing a Ziegler-Natta catalyst for the polymerization of olefins, is reproduced below:-

" a) Combining a spherical spray-cooled MgCl2-xROH support, wherein x is in the range from 1.5 to 6.0 and ROH is an alcohol or a mixture of alcohols where R is a linear, cyclic, or branched hydrocarbon unit with 1-10 carbon atoms, with a transition metal compound in a reactor at a temperature of between -30°C and +40°C;
b) heating the mixture in the reactor to a temperature of between 30°C to 100°C;
c) concurrent with the heating in step (b), or following reaching the temperature of step (b), adding an internal electron donor consisting essentially of a diether compound to the mixture in the reactor;
d) heating the resulting mixture to 80-125°C, if necessary, and holding the resulting mixture at that temperature for 1 to 3 hours to C.A.(COMM.IPD-PAT) 12/2023 Page 17 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 produce a precatalyst;
e) filtering the mixture containing the pre-catalyst while still hot to obtain the solid pre-catalyst component;
f) extracting the pre-catalyst with a mixture of an organic solvent and a transition metal at a temperature 100-135°C for 1-5 hours to form a catalyst; and
g) washing the catalyst with a hydrocarbon solvent and drying the catalyst under vacuum and/or elevated temperature of 30-100°C;

wherein the diether compound is selected such that the resulting solid catalyst component has an activity and hydrogen response suitable for the production of propylene polymers having a molecular weight distribution in the range from 5.75 to 9."

21. Additionally, there is no cavil that a Co-ordinate Bench of this Court in Agriboard International vs LLC Deputy Controller of Patents and Designs19 while dealing with cases where a prior art document is cited and any order of rejection by the Controller for lack of inventive step has to also discuss/ describe the manner in which subject invention would be obvious to a person skilled in the art. The relevant extracts thereof are reproduced as hereinbelow:-

"24. In the opinion of this Court, while rejecting an invention for lack of inventive step, the Controller has to consider three elements-
                                      •     the invention disclosed in the prior art,
                                      •     the invention disclosed in the application under consideration, and
                                      •    the manner in which subject invention would be obvious to a
                                      person skilled in the art."

22. Applying the aforesaid to the facts of the present case, this Court finds that the Controller has discussed (i) about the prior art; as also (ii) about the invention made in the subject application; and lastly (iii) how the invention in 19 2022 SCC OnLine Del 940 C.A.(COMM.IPD-PAT) 12/2023 Page 18 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 the patent application is obvious to the person skilled in the art is evident from the below relevant extracts reproduced as under:-
"4. Objections A. Invention u/s 2(1)(j) I. The present invention lacks inventive step as Dl-D3 discloses the polymerisation of polypropylene with the catalyst comprising nonsubstituted and substituted 1,3 -propane diethers and derivatives of the group of succinates/ 2-isopentyl-2- isopropyl-1, 3- dimethoxypropane. Hence, for the person skilled in the art, it is obvious to reach a subject matter of the present application by mosaicing above-cited documents DI -D3. Therefore in the view of the above documents, claim 1-10 does not constitute an inventive step under section 2(1)(ja) of Patents Act,1970. Reference is to be taken from these documents: Dl: EP 1840138 Al D2: EP 1609805 Al D3: WO 2009152268 Al The present application discloses improved Ziegler Natta catalysts and methods of making the same. The Ziegler Natta catalyst is formed using a spherical MgCI xR0H support, where R is a linear cyclic or branched hydrocarbon unit with 110 carbon atoms and where ROH is an alcohol or a mixture of at least two different alcohols and where x has a range of about 1.5 to 6.0 preferably about 2.5 to 4 more preferably about 2.9 to 3.4 and even more preferably 2.95 to 3.35. The Ziegler Natta catalyst includes a Group 4, 8 transition metal and an internal donor comprising a diether compound. The catalyst has improved activity in olefin polymerization reactions as well as good stereoregularity and hydrogen sensitivity and may be useful in the production of phthalate-free propylene polymers having a molecular weight distribution (PI(GPC)) in the range from about 5.75 to about 9. DI discloses in its examples 13 and 15, the polymerisation of propylene in the presence of a catalyst comprising MgCl2.nROH, TiCI4 and 2-isobutyl-2-isopropyl-1, 3- dimethoxypropane. The polymers prepared have a MWD (GPC) of 7.
D2 discloses the polymerisation of propylene with catalysts comprising MgCl2.nROH; TiCI4 and 2- isopentyl-2- isopropyl-1, 3- dimethoxypropane or 9,9 bis(methoxymethyl)fluorene. The obtained PP have an MWD(GPC) of 7 or 7.1.
C.A.(COMM.IPD-PAT) 12/2023 Page 19 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06
D3 discloses the process as present claim 2 but for an internal electron donor (ED) in general. In the examples, DIBP is used but according to the description (see [40J), diether such as 1, 3 propane diethers can also be used in the process of D3. A further group of suitable internal donor compounds are nonsubstituted and substituted (1, 3 -propane diethers and derivatives of the group of succinates. The preparation of the particulate solid component, the internal electron donor compound in general is used in an amount of from about 0.01 to about 2 mole, preferably from about 0.04 to about 0.6 moles, more preferably from about 0.05 to about 0.2 mole for each mole of the magnesium halide compound.
B. Other Requirement(s) 1. 1. Claims of this application No. 4278/DELNP/2015 conflicts with the claims of application No. 4277/DELNP/2015, therefore the claims of this application can not be allowed as to avoid duplicate inventions.
C. Scope
1. Claims 2-10 are inconsistent and beyond the scope of claim 1.
xxx xxx
5. OBSERVATIONS
1. In view of discussions held during hearing, agent had filed written submissions and relevant documents on 8th October, 2021 with petition for extension of time. Written submissions filed with reference to the objections contained in hearing notice cannot be reproduced here for the sake of brevity and which can be seen in electronic filewrapper of the present Application on the official website of Intellectual Property India www.ipindia.gov.in.
6. The subject matter of revised claims 1-9 filed alongwith submission is directed towards the A process for producing a Ziegler- Natta catalyst for the polymerization of olefins. The claim 1 is as follows:-
1. A process for producing a Ziegler-Natta catalyst for the polymerization of olefins comprising the steps of: a. combining a spherical spray-cooled MgC12-x.ROH support, wherein x is in the range of from 1.5 to 6.0 and ROH is an alcohol or a mixture of alcohols where R is a linear, cyclic, or branched hydrocarbon unit C.A.(COMM.IPD-PAT) 12/2023 Page 20 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 with 1- 10 carbon atoms, with a C and'transition metal compound in a reactor at a temperature of between -30 C;°+40 C;°C to 100°b. heating the mixture in the reactor to a temperature of between 30 c. concurrent with the heating in step... ...
xxx xxx The key inventive features of the present invention as well as the problem to be solved can only be regarded as the provision of an alternative process for producing a Ziegler Natta catalyst suitable for the production of propylene polymers having a molecular weight distribution in the range of 5.75 to 9.
Example 13 of D1 is regarded as the closest prior art for present claim 1 as the catalyst described therein allows the preparation of polypropylene with a molecular weight distribution of 7, which is included in the range 5.75 to 9 as targeted by the present invention. The processes disclosed in examples 8, 10 and 14 of D2 disclose polypropylenes having a molecular weight distribution of 7 or 7.1 which is included in the range 5.75 to 9 as targeted by the present invention.
The document D3 (the applicant's own invention) discloses exactly the same process as presently claimed, except that the electron donor is more generally defined (see claims 1, 15 and paragraphs [0018]- [0028]), indicating that the spherical MgCl2-xROH support has more preferably a d50 of 40 to 90 microns which may be produced by the spray-cooling method and paragraph [0061] where a sixty micron (d50) MgCl2.3.2EtOH support is used, which appears to be the same as in the examples of present application, the skilled person would use such a support in the process of example 13 of D1 and add an extraction step f) as disclosed in the general process of D3 and would arrive at the process of present claim 1."

23. In view thereof, this Court finds that arguments as advanced by Ms. Nidhi Raman are worthy and hold due merit. The use of diether compound as an internal electron donor and the filtration of a heated reaction mixture to produce a catalyst for making propylene with specific molecular weight C.A.(COMM.IPD-PAT) 12/2023 Page 21 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 distribution (5.75 to 9) by the appellant in light of the cited prior art documents D1, D2 and D3 shows apparent overlap.

24. Example 13 of the cited prior art document D1 also elucidates preparation of propylene with a molecular weight distribution falling within the range targeted by the present patent application (5.75 to 9) and the catalyst preparation process that shares similarities with the present patent application as also use of same internal electron donor, 2-isobutyl-2- isopropyl-1, 3-dimethoxypropane and involves step of hot filtration. Relevant extracts of the said cited prior art document D1 is reproduced as under:-

"[0074] Among these, preferred are 1,3-diethers, and particularly preferred are 2-isopropyl-2-isobutyl-1,3-dimethoxypropane, 2,2- diisobutyl-1,3-dimethoxypropane, 2-isopropyl-2-isopentyl-1,3- dimethoxypropane, 2,2-dicyclohexyl-1,3- dimethoxypropane and 2, 2- bis(cyclohexylmethyl)-1,3-dimethoxypropane. [0075] These compounds may be used alone or in combination of two or more kinds thereof."

25. Moreover, Examples 8, 10 and 14 of the cited prior art document D2 specifically offer preparation of catalyst yielding polypropylene with similar molecular weight distribution i.e., 7 or 7.1 which falls within the ambit of this subject application.

26. Similarly, the cited prior art document D3, of the very same Inventor also describes a process exactly identical to the one claimed in the subject application, albeit with only minor distinctions in the broader definition of electron donor.

27. Resultantly, when combining process steps and parameters of the cited prior art document D3 with the disclosures made in the cited prior art C.A.(COMM.IPD-PAT) 12/2023 Page 22 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 documents D1 and D2, which elucidate diether compounds as internal electron donor and hot filtration, the invention disclosed in the present patent application emerges as a predictable outcome. As such a person skilled in the art, would employ the teachings in the cited prior art document D1 and the general process in the cited prior art document D3 to come to the Claim(s) outlined in the present subject application.

28. For better elucidation Examples and Claims made in the cited prior art documents D1 and D3 with the Claim made in the subject application are reproduced as under:-

                                  D1                     D3                 D3 second           Invention in the
                                                                           embodiment         Subject Application
                           [0200] First, in     [0024] a) Reacting the   [0030]        a)   a).     Combining       a
                           the same manner      MgC12-xROH        with   preparing      a   spherical spray-cooled
                           as in Example 1,     neat TiC14 at -30°C      cooled portion     MgCl2-xROH support,
                           2.8 mol of ethanol   to     +40°C,    more    of neat TiC14 or   wherein x is in the
                           was coordinated      preferably at -20C to    of TiC14 diluted   range from 1.5 to 6.0
                           to 1 mol of          +20C, even more          with    a   non    and ROH is an alcohol
                           magnesium            preferably between -     aromatic           or a mixture of alcohols
                           chloride to obtain   10C and +10C by          hydrocarbon.       where R is a linear,
                           a solid adduct.      slow addition of the                        cyclic, or branched
                                                TiC14 to the MgC12-                         hydrocarbon unit with
                                                xR0H/ organic solvent                       1- 10 carbon atoms,
                                                suspension       while                      with a transition metal
                                                providing     constant                      compound in a reactor
                                                stirring.                                   at a temperature of
                                                                                            between -30°C and
                                                                                            +40°C;
                           [0201] 46.2 mmol     [0025] b) Increasing     [0031]        b)   b).     heating       the
                           of    the    solid   the temperature of the   reacting     the   mixture in the reactor to
                           adduct, in terms     above         reaction   neat or diluted    a     temperature      of
                           of     magnesium     mixture to between       TiC14 at -30°C     between 30°C to 100°C;
                           atom, which was      about 30 °C and 100      to +40°C, more
                           suspended in 30      °C,         preferably   preferably at -
                           ml of decane, was    between about 40 and     20°C to +20°C,

                          C.A.(COMM.IPD-PAT) 12/2023                                                 Page 23 of 33
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                            wholly introduced     90 ° C, followed by       most preferably
                           to 200 ml of          addition of an internal   between -10°C
                           titanium              electron donor and        and +10°C by
                           tetrachloride         continuing to heat the    slow addition of
                           which           was   mixture to at least 80°   the preformed,
                           maintained at -       C for about 1 to 2        spherical
                           20°C,         under   hours.                    particles     of
                           stirring.       The                             MgC12-xROH
                           temperature      of                             while providing
                           the mixed solution                              constant
                           was elevated to                                 stirring.
                           80°C      over    5
                           hours. When the
                           temperature
                           reached 80°C, 2-
                           isobutyl-2-
                           isopropyl-1,3-
                           dimethoxypropan
                           e was added
                           thereto     in    a
                           proportion of 0.15
                           mol, based on 1
                           mol of magnesium
                           atom in the solid
                           adduct, and then
                           the temperature
                           thereof         was
                           elevated to 120°C
                           over 40 minutes.
                           When            the
                           temperature
                           reached 120°C,
                           diethyl          4-
                           cyclohexene-1,2-
                           dicarboxylate
                           (trans-isomer)
                           was added thereto
                           in a proportion of
                           0.15 mol, based
                           on 1 mol of
                           magnesium atom

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                            in      the     solid
                           adduct, and then
                           the temperature
                           thereof          was
                           maintained         at
                           120°C over 90
                           minutes        under
                           stirring.
                           [0202] After the        [0026] c) Filtering the   [0032]          c)   c).     concurrent with
                           completion of the       reaction mixture at       increasing the       the heating in step (b),
                           reaction for 90         room temperature to       temperature of       or following reaching
                           minutes, a solid        obtain    the     solid   the      reaction    the temperature of step
                           portion          was    precatalyst.              mixture         to   (b), adding an internal
                           recovered by hot                                  about 30 to          electron          donor
                           filtration.      This                             100°C,               consisting essentially of
                           solid portion was                                 preferably      to   a diether compound to
                           resuspended        in                             about 40 to          the mixture in the
                           200 ml of titanium                                90°C, followed       reactor;
                           tetrachloride, and                                by addition of
                           the temperature                                   an       internal
                           thereof          was                              electron donor
                           elevated           to                             and continuing
                           130°C, and then                                   to heat the
                           maintained at that                                mixture to at
                           temperature                                       least 80°C.
                           under stirring for
                           45 minutes to
                           effect      reaction.
                           After             the
                           completion of the
                           reaction for 45
                           minutes, a solid
                           portion          was
                           recovered again
                           by hot filtration.
                           The       recovered
                           solid portion was
                           sufficiently
                           washed           with
                           decane           and
                           heptane at 100°C

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                            until     a     free
                           titanium
                           compound was no
                           longer detected in
                           the        washing
                           solution.
                           [0203] Thus, the       [0027] d) Extracting     [0033]        d)   d).     heating      the
                           solid      titanium    the precatalyst using    filtering    the   resulting mixture to 80-
                           catalyst               the Soxhlet extraction   reaction mixture   125°C, if necessary,
                           component (a13)        method      employing    at         room    and      holding     the
                           which           was    TiC14             and    temperature        resulting mixture at
                           prepared in the        ethylbenzene (at a                          that temperature for 1
                           above procedure        volume ratio of about                       to 3 hours to produce a
                           was stored as a        30:70,      preferably                      precatalyst;
                           decane slurry. An      20:80,           most
                           aliquot portion of     preferably 10:90) for
                           the slurry was         1-5 hours, preferably
                           picked and dried       1-4    hours,    most
                           to examine the         preferably 1-3 hours
                           catalyst               at a temperature of at
                           composition.           least          100°C,
                           [0204]          The    preferably 100-135°C
                           composition       of   most preferably 120-
                           the thus obtained      130°C.
                           solid      titanium
                           catalyst
                           component (a13)
                           was such that
                           titanium was 2.0
                           mass%,
                           magnesium was
                           19          mass%,
                           chlorine was 60
                           mass%, and an
                           ethanol residue
                           was 0.2 mass%.
                           [0205]      To     a   [0028] e) cooling the    [0034]         e) e).    filtering    the
                           polymerization         catalyst   to   room     Extracting    the mixture containing the
                           vessel with an         temperature (20°C),      precatalyst       pre-catalyst while still
                           internal volume of     washing several times    using         the hot to obtain the solid
                           2 liters, 500 g of     with a                   Soxhlet           pre-catalyst

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                            propylene, and 1     hydrocarbon       like   extraction        component;
                           NL of hydrogen       pentane, hexane or       method
                           were added at        heptane, and then        employing
                           room                 drying under vacuum      TiC14        and
                           temperature, and     and/or elevated          ethylbenzene (at
                           then 0.5 mmol of     temperature of 30-       a volume ratio
                           triethylaluminum,    100°C, preferably 40-    of about 30:70,
                           0.1     mmol    of   90°C, most preferably    preferably
                           cyclohexylmethyl     50-80 °C.                20:80,       most
                           dimethoxysilane                               preferably
                           and 0.004 mmol,                               10:90) for 1-5
                           in     terms    of                            hours,
                           titanium atom, of                             preferably 1-4
                           the solid catalyst                            hours,       most
                           component (a13)                               preferably 1-3
                           were         added                            hours     at   a
                           thereto, and the                              temperature of
                           internal                                      at least 100°C,
                           temperature     of                            preferably 100-
                           the                                           135°C        most
                           polymerization                                preferably 120-
                           vessel was rapidly                            130°C.
                           elevated to 70°C.
                           After
                           polymerization at
                           70°C for 1 hour,
                           a small amount of
                           methanol       was
                           added thereto to
                           stop the reaction,
                           and      propylene
                           was purged. The
                           obtained polymer
                           particles     were
                           dried        under
                           reduced pressure
                           overnight       at
                           80°C.
                           [0205]     To    a                            [0035]          f) f).   extracting the
                           polymerization                                Cooling       the pre-catalyst with a
                           vessel with an                                catalyst to room mixture of an organic

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                            internal volume of          temperature        solvent and a transition
                           2 liters, 500 g of          (20°C), washing    metal at a temperature
                           propylene, and 1            several    times   100-135°C for 1-5
                           NL of hydrogen              with           a   hours to form a
                           were added at               hydrocarbon,       catalyst; and
                           room                        like    pentane,
                           temperature, and            hexane        or
                           then 0.5 mmol of            heptane,     and
                           triethylaluminum,           then      drying
                           0.1     mmol    of          under vacuum
                           cyclohexylmethyl            and/or elevated
                           dimethoxysilane             temperature of
                           and 0.004 mmol,             30-100°C,
                           in     terms    of          preferably 40-
                           titanium atom, of           90°C,       most
                           the solid catalyst          preferably 50-
                           component (a13)             80 °C.
                           were         added
                           thereto, and the
                           internal
                           temperature     of
                           the
                           polymerization
                           vessel was rapidly
                           elevated to 70°C.
                           After
                           polymerization at
                           70°C for 1 hour,
                           a small amount of
                           methanol       was
                           added thereto to
                           stop the reaction,
                           and      propylene
                           was purged. The
                           obtained polymer
                           particles     were
                           dried        under
                           reduced pressure
                           overnight       at
                           80°C.
                           [0206]         The                             g).    washing           the

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                            activity of the                                        catalyst     with      a
                           catalyst, and the                                      hydrocarbon      solvent
                           MFR, the content                                       and drying the catalyst
                           of the decane-                                         under vacuum and/or
                           insoluble                                              elevated temperature of
                           components, the                                        30-100°C; wherein the
                           bulk       specific                                    diether compound is
                           gravity, and the                                       selected such that the
                           molecular weight                                       resulting solid catalyst
                           distribution                                           component has an
                           (Mw/Mn, Mz/Mw)                                         activity and hydrogen
                           of the obtained                                        response suitable for
                           polymer      were                                      the     production    of
                           shown in Table 1.                                      propylene      polymers
                                                                                  having a molecular
                                                                                  weight distribution in
                                                                                  the range from 5.75 to
                                                                                  9.
                                                                                      [Emphasis Supplied]

29. From the above, it is borne out that the process of obtaining the catalyst in the subject application is similar to that in the cited prior art documents.

30. In the impugned order, the Controller has applied the Could-Would approach to test the obviousness and hold that a person skilled in the art "...would use such a support in the process of example 13 of D1 and add an extraction step as disclosed in the general process of D3 and would arrive at the process of present claim 1. ...". The same is of utmost relevance since one of the inventors, Mr. Winter Andreas is common in both the cited prior art document D3 is the same as in this subject application. The said Mr. Winter Andreas is himself a person skilled in the art who would have been aware of all that what was involved therein. It is of utmost relevance since a C.A.(COMM.IPD-PAT) 12/2023 Page 29 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 person skilled in the art, as per settled law, is a normal skilled and ordinary person having all the knowledge available to public at the priority date in the specific field as the invention in the patent application. [Re.: F. Hoffmann- La Roche Ltd. & Anr. vs. Cipla Ltd. (Supra)]. It is also of relevance that all the cited prior art documents D1, D2 and D3 were available prior to the subject application. Thus, the aforesaid read with the Claims made in the subject application gives an impression that the appellant is attempting to monopolise and evergreen the patent, which cannot be allowed since it will tantamount to evergreening and would give a rebirth to the patent after end of its fixed term. The same is not permissible, even otherwise, since it is an admitted fact that a mere inventive step does not/ cannot always give rise to a new/ fresh invention in a patent, the same also has to be not obvious to a person skilled in the art.

31. Under these circumstances, the claim of the appellant that the subject application relates to a Ziegler-Natta catalyst, particularly, an improved method for making a Ziegler-Natta catalyst essentially using diether compounds as internal donor holds no water, firstly, since the appellant did not provide any studies demonstrating that the properties of the catalyst, including its activity and hydrogen response which as per it, is solely attributed to use of diether compounds as internal donors, and secondly, since the Controller had already granted patent application bearing no.4277/DELNP/2015 of the appellant filed along with the present patent application on the very same day, which was also featuring a similar Ziegler- Natta catalyst with silica as the carrier and employing similar 1,3-diether C.A.(COMM.IPD-PAT) 12/2023 Page 30 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 compounds as internal donors. The appellant is unable to demonstrate any difference(s) inter-se the two-patent application(s) so filed by the appellant.

32. This Court finds that the Controller has passed a well-reasoned order qua non-patentability of an invention under Section 2(1)(ja) of the 1970 Act as noted hereinabove, this itself shows a clear application of mind by the Controller. Furthermore, the impugned order having satisfied the tests laid down in Agriboard (supra) and has not been passed in a routine and/ or casual manner. Reliance is placed upon Dolby International AB (supra) wherein it has been held as under:-

"9. It would well for the officers in the office of the Controller of Patents and Designs, who are discharging such functions, to bear in mind the fact that grant or rejection of a patent is a serious matter. A patent is meant to be a recognition of the innovative step that has been put into a crafting of an invention. Inventions increment the state of existing scientific knowledge and, thereafter, are of inestimable public interest. Any decision, whether to grant or refuse a patent has, therefore, to be informed by due application of mind, which must be reflected in the decision. Orders refusing applications for grant of a patent cannot be mechanically passed, as has been done in the present case."

[Emphasis Supplied]

33. Therefore, in view of the aforesaid, it cannot be said that the cited prior art document D3 teaches away from the invention claimed in the present patent application and any person skilled in the art would lack motivation to combine the cited prior art documents D1, D2 and D3 as the said person skilled in the art would be aware of all the prior art(s) in the said field. So, as borne out from the above, all the cited prior art documents D1, D2 and D3 are qua the subject matter of same field as the subject application and as such are interlinked.

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34. Lastly, the contention that the cited prior art document D3 teaches away from diether as electron donors is incorrect because the said test requires that prior art should suggest the certain approach or solution would not work or is not advisable. Though the said cited prior art document D3 lists diether as suitable electron donor but nowhere does it mention diether as non-suitable solution or that it would not work and a person skilled in the art would be discouraged from following to use the same as internal donor. In any event, the said cited prior art document D3 has to be seen as a whole and there is no teaching away [Re:. F. Hoffmann-La Roche Ltd. & Anr. vs. Cipla Ltd. 2015 SCC OnLine Del 13619]. The relevant extracts of document D3 are reproduced as under:-

"[0012] The catalyst includes a Group 4-8 transition metal, such as Ti, and an internal donor like aromatic esters, diethers, succinates, or hindered amines, preferably dialkylphthalates like diisobutylphthalate (D- i-BP) or di-n-butylphthalate (D-n-BP). The catalyst of the present invention has improved activity in olefin polymerization reactions as well as good stereoregularity and hydrogen sensitivity.
xxx xxx [0038] The internal electron donors referenced in the procedure are typically a Lewis base. Suitable electron donors include diesters, diethers and succinates. Preferred internal donor compounds included carboxylic acid derivatives and in particular phthalic acid derivatives having the general formula:... ...
xxx xxx [0040] A further group of suitable internal donor compounds are the non- substituted and substituted (CI-CIO alkyl)-1,3-propane diethers and derivatives of the group of succinates.
xxx xxx C.A.(COMM.IPD-PAT) 12/2023 Page 32 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06 [0042] Also, mixtures of two or more internal electron donor compounds may be used in the preparation of the solid catalytic comsponent of the invention."

[Emphasis Supplied]

35. As such, there is no ground made out for setting aside the well- reasoned impugned order in line with law as also existing various precedent laid down by this Court, more so, since both the process and the product are covered by the cited prior art documents D1, D2 and D3 and the invention in the subject application is obvious to the person skilled in the art under Section 2(1)(ja) of the 1970 Act. In view thereof, the judgments cited by Ms. Vindhya S. Mani, learned counsel for the appellant, are not applicable to the facts of the present case involving the subject application.

36. Accordingly, the present appeal is dismissed, leaving the parties to bear their own costs.

37. The Registry is directed to supply a copy of this judgment to the office of the Controller General of Patents, Designs & Trade marks of India on llc- [email protected] for information.

SAURABH BANERJEE, J.

MAY 29, 2025/Ab C.A.(COMM.IPD-PAT) 12/2023 Page 33 of 33 Signature Not Verified Digitally Signed By:BABLOO SHAH Signing Date:29.05.2025 17:57:06