Prosecution Insights
Last updated: July 17, 2026
Application No. 18/549,406

METHOD FOR PREPARATION OF AMIDINES

Non-Final OA §103
Filed
Sep 07, 2023
Priority
Mar 08, 2021 — IT 102021000005321 +1 more
Examiner
HAVLIN, ROBERT H
Art Unit
1626
Tech Center
1600 — Biotechnology & Organic Chemistry
Assignee
VERSALIS S.P.A.
OA Round
2 (Non-Final)
52%
Grant Probability
Moderate
2-3
OA Rounds
0m
Est. Remaining
80%
With Interview

Examiner Intelligence

Grants 52% of resolved cases
52%
Career Allowance Rate
535 granted / 1033 resolved
-8.2% vs TC avg
Strong +28% interview lift
Without
With
+27.7%
Interview Lift
resolved cases with interview
Typical timeline
2y 9m
Avg Prosecution
83 currently pending
Career history
1134
Total Applications
across all art units

Statute-Specific Performance

§101
0.7%
-39.3% vs TC avg
§103
37.5%
-2.5% vs TC avg
§102
14.2%
-25.8% vs TC avg
§112
32.0%
-8.0% vs TC avg
Black line = Tech Center average estimate • Based on career data from 1033 resolved cases

Office Action

§103
Notice of Pre-AIA or AIA Status The present application, filed on or after March 16, 2013, is being examined under the first inventor to file provisions of the AIA . Priority This application is a 371 of PCT/IB2022/051869 (03/03/2022) and claims foreign priority to ITALY 102021000005321 (03/08/2021). Status Rejections not reiterated in the action are withdrawn. New Claim Rejections - 35 USC § 103 Claims 1-13 and 16 are rejected under 35 U.S.C. 103 as being unpatentable over Bi et al. (CN101279973, citations to English translation) in view of Zhen et al. (CN1546492A (2004-11-17, machine translation)), Formenti et al. (Chem. Eur. J. 2020, 26, p. 15589 – 15595, p. S1-S46), and Johnson-Matthey (Chemical Catalyst – Product List, 2013, 6 pages). Bi teaches the synthesis of 1.8-diaminebicyclo(5,4,0)-7-undecene (DBU) (corresponding to instant claim 1’s formula (V)) in three steps: addition - caprolactam (corresponding to instant claim 1’s formula (I)) and acrylonitrile (corresponding to instant claim 1’s formula (II)) in t-butanol with catalytic NaOH to form cyanoethyl caprolactam (corresponding to instant claim 1’s formula (III)) at 10-50C; hydrogenation of the formed cyanoethyl caprolactam directly in the same solvent using a Raney-Ni catalyst under 5 MPa hydrogen at 115C to form the amine (corresponding to instant claim 1’s formula (IV)); and cyclization/dehydration with a p-toluenesulfonic acid at 150-180C (Abstract, pages 1-4). Bi differs from claim 1 by the catalysts used – i.e., Raney-Ni vs. the claim’s “not of the Raney type or of the sponge type”. Zhen teaches the synthesis of 1.8-diaminebicyclo(5,4,0)-7-undecene (DBU) (corresponding to instant claim 1’s formula (V)) in three steps: A) caprolactam (corresponding to instant claim 1’s formula (I)) and acrylonitrile (corresponding to instant claim 1’s formula (II)) in toluene with catalytic NaOH or KOH to form cyanoethyl caprolactam (corresponding to instant claim 1’s formula (III)) at 50-60C; B) hydrogenation of cyanoethyl caprolactam using an “catalyst of Al, Ni, Fe, and Cr” “prepared in a mass percentage ratio of 50:40:7:3” under hydrogen at 90-120C to form the amine (corresponding to instant claim 1’s formula (IV)); and C) cyclization with a “0.5-2 wt% of catalyst antimony trioxide” at 150-160C (Abstract, claims 1-2). Formenti teaches Co catalysts for “efficient and general nitrile hydrogenation” that “outperformed all other tested commercial catalysts, for example, Raney Nickel” (title, abstract). Johnson-Matthey teaches commercially available catalysts including “HTC CO 2000 RP 1.2” for “hydrogenation of nitriles” (p. 4). One of ordinary skill in the art following the teaching of Bi and Zhen would have considered utilizing different catalysts known in the art for hydrogenation of nitriles such as those taught by Formenti and Johnson-Matthey. One of ordinary skill in the art would have been motivated to substitute a catalysts because such modifications are routinely done to employ improved efficiency catalysts and commercially available catalysts. Furthermore, such a modification is a substitution of a known equivalent which is prima facie obvious. MPEP 2144.06. Thus, claims 1-3, 6-10 are obvious. Regarding claim 4, Bi teaches in Example 1, 50.2g acrylonitrile to 100g caprolactam is (0.95:0.88 = 1.08). Regarding claim 5, Bi teaches in Example 1 step A at 40C and at atmospheric pressure. Regarding the time of reaction, Bi teaches 1 hour. Regarding claim 11, Zhen teaches the reaction is performed in a reactor with stirring such the one of skill in the art would at once envisage a stirred reactor CSTR. MPEP 2131.02.III. Regarding claim 12, Bi teaches the use of p-toluenesulfonic acid in the condensation reaction but does not teach the claimed solvent. Formenti teaches the hydrogenation reaction is general across a variety of solvents including xylene which one of ordinary skill in the art would have considered given the success of the prior art. Regarding claim 13, Bi teaches a heterogenous catalyst based on resins. Regarding claim 16, the combined teaching of the prior art teaches hydrogenation in the absence of ammonia and in the presence of water and one of ordinary skill in the art would have routinely optimized the solvent, ratios, temperature, and pressure as these are all well-known results effective variable in the optimization of products in a synthetic scheme. Claims 14-15 are rejected under 35 U.S.C. 103 as being unpatentable over Bi et al. (CN101279973, citations to English translation) in view of Zhen et al. (CN1546492A (2004-11-17, machine translation)), Formenti et al. (Chem. Eur. J. 2020, 26, p. 15589 – 15595, p. S1-S46), Johnson-Matthey (Chemical Catalyst – Product List, 2013, 6 pages) as applied to claims 1-13 and 16 above and further in view of Couper (Chemical Process Equipment, 3rd ed., 2012, 838 pages). Regarding claim 14 to a continuous process in a solvent of xylene, one of ordinary skill in the art would have considered scaling up the obvious process for production of the commercially important pharmaceutical intermediate of DBU in a continuous process using xylene as a solvent with a reasonable expectation of success. Regarding claim 15, the modified teaching of the prior art does not teach scaling up the reaction to industrial scale. However, Couper teaches reactor design including evaporators, distillation columns, heat exchangers, fixed bed and trickle bed reactors, and the significance of WHSV which were all well-known in the art and are part of the requisite in reaction optimization when scaling up. Thus, one of ordinary skill in the art following the teaching of the prior art utilizing their high level of skill in view of the well-known techniques of scaling up reactions would have arrived at the claimed invention with a reasonable expectation of success. With each of the claims, the level of skill in the art is very high such that one of ordinary skill in the art would consider routine the combination of elements from the teaching of the art. One of ordinary skill in the art would have recognized that the results of the combination would be predictable due to the well-known nature and optimizations routinely performed in the art. Thus, one of ordinary skill in the art would have arrived at the invention as claimed before the effective filing date with a reasonable expectation of success. New Double Patenting Claims 1-16 are provisionally rejected on the ground of nonstatutory double patenting as being unpatentable over claims 1-11 of copending Application No. 18549412 (reference application) in view of Bi et al. (CN101279973, citations to English translation) in view of Zhen et al. (CN1546492A (2004-11-17, machine translation)), Formenti et al. (Chem. Eur. J. 2020, 26, p. 15589 – 15595, p. S1-S46), Johnson-Matthey (Chemical Catalyst – Product List, 2013, 6 pages). Although the claims at issue are not identical, they are not patentably distinct from each other because the reference application claims the synthesis of the same product as in the instant application such that one of ordinary skill in the art would find using the same intermediates in the same fashion in view of the prior art as detailed in the 35 USC 103 rejection supra and arrive at the claimed invention with a reasonable expectation of success. This is a provisional nonstatutory double patenting rejection because the patentably indistinct claims have not in fact been patented. Conclusion No claims allowed. Applicant's amendment necessitated the new ground(s) of rejection presented in this Office action. Accordingly, THIS ACTION IS MADE FINAL. See MPEP § 706.07(a). Applicant is reminded of the extension of time policy as set forth in 37 CFR 1.136(a). A shortened statutory period for reply to this final action is set to expire THREE MONTHS from the mailing date of this action. In the event a first reply is filed within TWO MONTHS of the mailing date of this final action and the advisory action is not mailed until after the end of the THREE-MONTH shortened statutory period, then the shortened statutory period will expire on the date the advisory action is mailed, and any nonprovisional extension fee (37 CFR 1.17(a)) pursuant to 37 CFR 1.136(a) will be calculated from the mailing date of the advisory action. In no event, however, will the statutory period for reply expire later than SIX MONTHS from the mailing date of this final action. Any inquiry concerning this communication or earlier communications from the examiner should be directed to ROBERT H HAVLIN whose telephone number is (571)272-9066. The examiner can normally be reached 9am - 6pm. Examiner interviews are available via telephone, in-person, and video conferencing using a USPTO supplied web-based collaboration tool. To schedule an interview, applicant is encouraged to use the USPTO Automated Interview Request (AIR) at http://www.uspto.gov/interviewpractice. If attempts to reach the examiner by telephone are unsuccessful, the examiner’s supervisor, Kortney Klinkel can be reached at (571) 270-5293. The fax phone number for the organization where this application or proceeding is assigned is 571-273-8300. Information regarding the status of published or unpublished applications may be obtained from Patent Center. Unpublished application information in Patent Center is available to registered users. To file and manage patent submissions in Patent Center, visit: https://patentcenter.uspto.gov. Visit https://www.uspto.gov/patents/apply/patent-center for more information about Patent Center and https://www.uspto.gov/patents/docx for information about filing in DOCX format. For additional questions, contact the Electronic Business Center (EBC) at 866-217-9197 (toll-free). If you would like assistance from a USPTO Customer Service Representative, call 800-786-9199 (IN USA OR CANADA) or 571-272-1000. /ROBERT H HAVLIN/Primary Patent Examiner, Art Unit 1626
Read full office action

Prosecution Timeline

Sep 07, 2023
Application Filed
Dec 10, 2025
Non-Final Rejection mailed — §103
Mar 02, 2026
Response Filed
Apr 03, 2026
Final Rejection mailed — §103
Jun 24, 2026
Response after Non-Final Action

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Study what changed to get past this examiner. Based on 5 most recent grants.

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Prosecution Projections

2-3
Expected OA Rounds
52%
Grant Probability
80%
With Interview (+27.7%)
2y 9m (~0m remaining)
Median Time to Grant
Moderate
PTA Risk
Based on 1033 resolved cases by this examiner. Grant probability derived from career allowance rate.

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