Prosecution Insights
Last updated: July 17, 2026
Application No. 18/417,188

PROCESS FOR PREPARING AN OLEFIN STREAM FOR OLIGOMERIZATION WITH DIMETHYL ETHER REMOVAL

Non-Final OA §103
Filed
Jan 19, 2024
Priority
Jan 20, 2023 — provisional 63/480,873
Examiner
STEIN, MICHELLE
Art Unit
1771
Tech Center
1700 — Chemical & Materials Engineering
Assignee
Uop LLC
OA Round
1 (Non-Final)
44%
Grant Probability
Moderate
1-2
OA Rounds
1y 3m
Est. Remaining
79%
With Interview

Examiner Intelligence

Grants 44% of resolved cases
44%
Career Allowance Rate
293 granted / 663 resolved
-20.8% vs TC avg
Strong +34% interview lift
Without
With
+34.5%
Interview Lift
resolved cases with interview
Typical timeline
3y 9m
Avg Prosecution
26 currently pending
Career history
722
Total Applications
across all art units

Statute-Specific Performance

§101
0.2%
-39.8% vs TC avg
§103
81.3%
+41.3% vs TC avg
§102
2.5%
-37.5% vs TC avg
§112
0.9%
-39.1% vs TC avg
Black line = Tech Center average estimate • Based on career data from 663 resolved cases

Office Action

§103
DETAILED ACTION 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 . Claim Rejections - 35 USC § 103 The following is a quotation of 35 U.S.C. 103 which forms the basis for all obviousness rejections set forth in this Office action: A patent for a claimed invention may not be obtained, notwithstanding that the claimed invention is not identically disclosed as set forth in section 102, if the differences between the claimed invention and the prior art are such that the claimed invention as a whole would have been obvious before the effective filing date of the claimed invention to a person having ordinary skill in the art to which the claimed invention pertains. Patentability shall not be negated by the manner in which the invention was made. The factual inquiries for establishing a background for determining obviousness under 35 U.S.C. 103 are summarized as follows: 1. Determining the scope and contents of the prior art. 2. Ascertaining the differences between the prior art and the claims at issue. 3. Resolving the level of ordinary skill in the pertinent art. 4. Considering objective evidence present in the application indicating obviousness or nonobviousness. This application currently names joint inventors. In considering patentability of the claims the examiner presumes that the subject matter of the various claims was commonly owned as of the effective filing date of the claimed invention(s) absent any evidence to the contrary. Applicant is advised of the obligation under 37 CFR 1.56 to point out the inventor and effective filing dates of each claim that was not commonly owned as of the effective filing date of the later invention in order for the examiner to consider the applicability of 35 U.S.C. 102(b)(2)(C) for any potential 35 U.S.C. 102(a)(2) prior art against the later invention. Claims 1-20 are rejected under 35 U.S.C. 103 as being unpatentable over Risch (US 2005/0043575) in view of Van Egmond (US 2004/0102669). Regarding claims 1-20, Risch teaches that C4+ olefin streams from MTO processes are fed to selective hydrogenation [0028-0031], [0016-0019], followed by oligomerization [0019], [0034-35]. Risch does not explicitly disclose the MTO process steps, or how the C4+ olefins are separated. However, Van Egmond teaches a similar process for selective hydrogenation of C4+ olefins recovered from MTO processes [0118]. Van Egmond separates the effluent from the MTO reactor by a quench device to separate water from light olefins, and dimethyl ether [0075-0077], followed by additional conventional separation devices to recover C4+ from the lighter materials [0108-0118]. Van Egmond additionally teaches using conventional demethanizers, deethanizer, depropanizer, wash towers, caustic tours, splitters, etc [0109]. Therefore, it would have been obvious the person having ordinary skill in the art to have separated water from the light olefins, followed by conventional separation such as stripping, as described by Van Egmond in order to recover the C4+ fraction to be fed to selective hydrogenation. Examiner notes that as disclosed by Van Egmond, it would have been obvious to the person having ordinary skill in the art to have selected appropriate separation equipment and steps in order to obtain the desired C4+ olefins to be fed to the selective hydrogenation step [0108-0118]. Conclusion The prior art made of record and not relied upon is considered pertinent to applicant's disclosure. Shutt (US 2004/0039239) – teaches MTO followed by separation, recover of C4+ components which are fed to hydrogenation (see figure 2) Van Egmond (US 2005/0033104) – teaches MTO, water wash, and separation of C4+ components Ding (US 2004/0267077) – teaches oxygenate to olefin reaction, quenching, washing, and olefin product recovery Schindlbeck (US 2020/0047079) - teaches separation of MTO effluent Xu (US 2005/0101815) – from ISR teaches oxygenate to olefin conversion and separation of effluents Martens (US 2005/0182282) – from ISR teaches C4+ from oxygenate to olefin reactor fed to oligomerization Any inquiry concerning this communication or earlier communications from the examiner should be directed to MICHELLE STEIN whose telephone number is (571)270-1680. The examiner can normally be reached Monday-Friday 8:30 AM-5:00 PM. 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, Prem C Singh can be reached at 571-272-6381. 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. /MICHELLE STEIN/Primary Examiner, Art Unit 1771
Read full office action

Prosecution Timeline

Jan 19, 2024
Application Filed
Apr 21, 2026
Non-Final Rejection mailed — §103 (current)

Precedent Cases

Applications granted by this same examiner with similar technology

Patent 12680034
METHODS AND SYSTEMS FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICAL PRODUCTS
2y 5m to grant Granted Jul 14, 2026
Patent 12680035
METHODS AND SYSTEMS FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICAL PRODUCTS
2y 5m to grant Granted Jul 14, 2026
Patent 12667831
PROCESSES AND BIMETALLIC CRACKING ADDITIVES FOR STEAM ENHANCED CATALYTIC CRACKING OF CRUDE OIL TO PRODUCE LIGHT OLEFINS AND AROMATICS
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Patent 12668555
METHOD FOR PREPARING ETHYLENE PROPYLENE
3y 3m to grant Granted Jun 30, 2026
Patent 12655360
METHOD AND APPARATUS FOR DESULFURIZATION AND SEPARATION OF CATALYTICALLY CRACKED LIGHT PRODUCT
4y 1m to grant Granted Jun 16, 2026
Study what changed to get past this examiner. Based on 5 most recent grants.

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Prosecution Projections

1-2
Expected OA Rounds
44%
Grant Probability
79%
With Interview (+34.5%)
3y 9m (~1y 3m remaining)
Median Time to Grant
Low
PTA Risk
Based on 663 resolved cases by this examiner. Grant probability derived from career allowance rate.

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