The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Apr. 16, 2024

Filed:

Oct. 30, 2022
Applicant:

Chevron U.s.a. Inc., San Ramon, CA (US);

Inventor:

Hye-Kyung Timken, Albany, CA (US);

Assignee:

CHEVRON U.S.A INC., San Ramon, CA (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 1/10 (2006.01); C07C 4/06 (2006.01); C08F 10/06 (2006.01); C10B 53/07 (2006.01); C10G 1/00 (2006.01); C10G 11/18 (2006.01); C10G 45/58 (2006.01); C10M 109/02 (2006.01); C10M 177/00 (2006.01); C10N 70/00 (2006.01);
U.S. Cl.
CPC ...
C10G 1/10 (2013.01); C07C 4/06 (2013.01); C08F 10/06 (2013.01); C10B 53/07 (2013.01); C10G 1/002 (2013.01); C10G 11/18 (2013.01); C10G 45/58 (2013.01); C10M 109/02 (2013.01); C10M 177/00 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/304 (2013.01); C10G 2300/305 (2013.01); C10G 2300/308 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/08 (2013.01); C10G 2400/10 (2013.01); C10G 2400/26 (2013.01); C10M 2203/003 (2013.01); C10N 2070/00 (2013.01);
Abstract

A continuous process for converting waste plastic into recycle for polypropylene polymerization is provided. The process integrates refinery operations to provide an effective and efficient recycle process. The process comprises selecting waste plastics containing polyethylene and polypropylene and then passing the waste plastics through a pyrolysis reactor to thermally crack at least a portion of the polyolefin waste and produce a pyrolyzed effluent. The pyrolyzed effluent is separated into offgas, a naphtha/diesel fraction, a heavy fraction, and char. The naphtha/diesel fraction is passed to a refinery FCC unit, from which is recovered a liquid petroleum gas Colefin/paraffin mixture. The Cparaffins and Colefins are separated into different fractions with a propane/propylene splitter. The Colefin fraction is passed to a propylene polymerization reactor. The Cparaffin fraction is optionally passed to a dehydrogenation unit to produce additional propylene and then the resulting Colefin is passed to a propylene polymerization reactor. The heavy fraction of pyrolyzed oil is passed to an isomerization dewaxing unit to produce a lubricating base oil.


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