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. 19, 2022

Filed:

Dec. 23, 2020
Applicant:

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

Inventors:

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

Cameron McCord, San Ramon, CA (US);

Assignee:

Chevron U.S.A. Inc., San Ramon, CA (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10B 53/07 (2006.01); C10G 51/04 (2006.01); C10G 57/02 (2006.01); C10G 31/06 (2006.01); C10G 35/02 (2006.01); C10G 51/02 (2006.01); C10G 9/36 (2006.01);
U.S. Cl.
CPC ...
C10B 53/07 (2013.01); C10G 9/36 (2013.01); C10G 31/06 (2013.01); C10G 35/02 (2013.01); C10G 51/023 (2013.01); C10G 57/02 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/1044 (2013.01); C10G 2400/06 (2013.01); C10G 2400/20 (2013.01); C10G 2400/28 (2013.01);
Abstract

Provided in one embodiment is a continuous process for converting waste plastic into recycle for polyethylene polymerization. The process comprises selecting waste plastics containing polyethylene and/or polypropylene, and 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 pyrolysis oil and optionally wax comprising a naphtha/diesel and heavy fraction, and char. The pyrolysis oil is passed to a refinery FCC unit from which a liquid petroleum gas Colefin/paraffin mixture fraction is recovered, as well as a Colefin/paraffin mixture fraction. The liquid petroleum gas Colefin/paraffin mixture fraction is passed to a steam cracker for ethylene production. The Colefin/paraffin mixture fraction is passed to a refinery alkylation unit, from which a n-butane and naphtha feed for a stream cracker to produce ethylene is recovered.


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