Prosecution Insights
Last updated: April 19, 2026
Application No. 18/573,056

SYSTEMS AND METHODS FOR PROCESSING MIXED PLASTIC WASTE

Non-Final OA §103
Filed
Dec 21, 2023
Examiner
NGUYEN, TAM M
Art Unit
1771
Tech Center
1700 — Chemical & Materials Engineering
Assignee
SABIC Global Technologies B.V.
OA Round
1 (Non-Final)
78%
Grant Probability
Favorable
1-2
OA Rounds
2y 9m
To Grant
88%
With Interview

Examiner Intelligence

Grants 78% — above average
78%
Career Allow Rate
746 granted / 963 resolved
+12.5% vs TC avg
Moderate +11% lift
Without
With
+10.9%
Interview Lift
resolved cases with interview
Typical timeline
2y 9m
Avg Prosecution
68 currently pending
Career history
1031
Total Applications
across all art units

Statute-Specific Performance

§101
0.1%
-39.9% vs TC avg
§103
51.2%
+11.2% vs TC avg
§102
16.7%
-23.3% vs TC avg
§112
18.7%
-21.3% vs TC avg
Black line = Tech Center average estimate • Based on career data from 963 resolved cases

Office Action

§103
3DETAILED ACTION 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 . Election/Restrictions Applicant’s election of Group I, claims 1, 3, 8–12, 20, 24, and 26 in the reply filed on 2/16/2026 is acknowledged. Because applicant did not distinctly and specifically point out the supposed errors in the restriction requirement, the election has been treated as an election without traverse (MPEP § 818.01(a)). Claim Rejections - 35 USC § 103 In the event the determination of the status of the application as subject to AIA 35 U.S.C. 102 and 103 (or as subject to pre-AIA 35 U.S.C. 102 and 103) is incorrect, any correction of the statutory basis (i.e., changing from AIA to pre-AIA ) for the rejection will not be considered a new ground of rejection if the prior art relied upon, and the rationale supporting the rejection, would be the same under either status. 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, 3, 8–12, 20, 24, and 26 are rejected under 35 U.S.C. §103 as being unpatentable over Humphreys et al. (US 2020/0071619 A1) in view of Evans (EP 0571163 A1). Humphreys teaches processing mixed plastic/polymeric material by extruding the material to form a melt stream (¶[0010]–[0017]), wherein chlorine-containing polymers undergo dechlorination/dehalogenation during processing (¶[0141]–[0143]), and further teaches staged extrusion/reactive processing corresponding to sequential treatment of the material (¶[0207]–[0214], ¶[0209]). Humphreys also teaches mixing the extrusion-derived material with a solvent to form a reaction mixture (¶[0010]–[0013]), wherein the solvent includes hydrocarbon oil additives (e.g., gas-oil, aromatic oils) that may act as oil-solvents (¶[0196], ¶[0264]), and performing catalytic depolymerization of the polymeric material followed by downstream separation via fractionation/distillation (¶[0218], ¶[0262]–[0264]). Humphreys does not teach the use of a multi-tray reactive distillation column as claimed. Evans teaches a reactive distillation column integrating reaction and separation, including a multi-tray column with reaction and distillation trays and introduction of feed streams onto trays (p. 3, lines. 5–9; p. 1; claims). It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to employ the reactive distillation column of Evans in place of, or in combination with, the separation step of Humphreys, because Evans teaches that integrating reaction and distillation within a multi-tray column improves mass and heat transfer, enhances conversion, and reduces equipment count, representing a known process intensification technique. Claim 3 Humphreys teaches removal of halogens (including chlorine) via conversion to inorganic species during processing (¶[0141]–[0143]). Claim 8 It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to inject a stripping gas such as steam or hydrogen into the process, because stripping gases are routinely used in extrusion and devolatilization processes to remove volatile components and enhance separation efficiency. Claim 9 Humphreys teaches hydrocarbon oil additives (e.g., gas-oil, aromatic oils) acting as solvents (¶[0196]). It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to employ hydrocarbon oils capable of hydrogen donation as hydrogen donor solvents in order to stabilize free radical species formed during depolymerization, as hydrogen donation from hydrocarbon media is a well-known mechanism in thermal and catalytic cracking processes and represents a predictable use of known materials for their established function. Claim 10 Humphreys teaches: transition metal catalysts (¶[0176]) sulfur-containing catalyst systems (sulfided catalysts) (Table 2) It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to employ gaseous hydrogen in conjunction with the disclosed transition metal sulfided catalyst systems, because such catalysts are conventionally used under hydrogen atmospheres to promote hydrogen transfer and stabilize reactive intermediates in hydroprocessing reactions, representing a predictable application of known techniques. Claim 11 It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to select molybdenum octoate or molybdenum naphthenate as the transition metal catalyst, because such molybdenum-based compounds are well-known catalyst precursors for forming active sulfided molybdenum catalysts used in hydroprocessing reactions, and selection of a specific molybdenum precursor represents a routine choice among known alternatives. Claim 12 It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to select butyl sulfide as the sulfur-containing compound, because sulfur-containing organic compounds such as sulfides are well-known for providing sulfur to form or maintain sulfided transition metal catalysts, and selection of a specific sulfide compound represents a routine choice among known sulfur sources used in hydroprocessing systems. Claim 20 It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to include a reboiler and recycle vaporized bottoms stream within the distillation column system, because such features are standard in distillation column operation to maintain vapor-liquid equilibrium and improve separation efficiency. Claim 24 It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to shred the mixed plastic waste prior to extrusion, because size reduction is a routine preprocessing step that improves handling and processing efficiency. Claim 26 It would have been obvious to one having ordinary skill in the art before the effective filing date of the claimed invention to include an upstream plug flow reactor prior to the distillation column, because staged reaction systems are well-known and use of different reactor configurations represents a predictable variation to optimize conversion and residence time. Conclusion Any inquiry concerning this communication or earlier communications from the examiner should be directed to TAM M NGUYEN whose telephone number is (571)272-1452. The examiner can normally be reached Mon - Frid. 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 571-273-6381. 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. /TAM M NGUYEN/Primary Examiner, Art Unit 1771
Read full office action

Prosecution Timeline

Dec 21, 2023
Application Filed
May 23, 2024
Response after Non-Final Action
Mar 24, 2026
Non-Final Rejection — §103 (current)

Precedent Cases

Applications granted by this same examiner with similar technology

Patent 12595428
PROCESS FOR DEPOLYMERIZATION OF SOLID MIXED PLASTIC
2y 5m to grant Granted Apr 07, 2026
Patent 12589376
CATALYTIC REACTOR FOR CRACKING WAX IN WASTE PLASTIC PROLYSIS PROCESS, CATALYTIC COMPOSITION FOR CRACKING WAX IN WASTE PLASTIC PYROLYSIS PROCESS, AND PRODUCTION METHOD THEREOF
2y 5m to grant Granted Mar 31, 2026
Patent 12589362
SUPPORT, ZEOLITE MEMBRANE COMPLEX, METHOD OF PRODUCING ZEOLITE MEMBRANE COMPLEX, AND SEPARATION METHOD
2y 5m to grant Granted Mar 31, 2026
Patent 12584070
METALLIC BASED HYDROCARBON PYROLYSIS
2y 5m to grant Granted Mar 24, 2026
Patent 12570588
DISTILLATE HYDROCRACKING PROCESS WITH A REVERSE ISOMERIZATION STEP TO INCREASE A CONCENTRATION OF N-PARAFFINS
2y 5m to grant Granted Mar 10, 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
78%
Grant Probability
88%
With Interview (+10.9%)
2y 9m
Median Time to Grant
Low
PTA Risk
Based on 963 resolved cases by this examiner. Grant probability derived from career allow rate.

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