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:
Nov. 19, 2024

Filed:

Apr. 12, 2022
Applicant:

Chevron Phillips Chemical Company Lp, The Woodlands, TX (US);

Inventors:

Ronald G. Abbott, Porter, TX (US);

Bruce D. Murray, Kingwood, TX (US);

Scott G. Morrison, Kingwood, TX (US);

Bradley T. Price, Kingwood, TX (US);

Assignee:

Chevron Phillips Chemical Company LP, The Woodlands, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 1/00 (2006.01); C07C 4/04 (2006.01); C08F 10/02 (2006.01); C10B 53/07 (2006.01); C10B 57/06 (2006.01); C10G 1/10 (2006.01); C10G 9/36 (2006.01); C10G 11/18 (2006.01); C10L 1/06 (2006.01); C10L 1/08 (2006.01); C10L 3/06 (2006.01);
U.S. Cl.
CPC ...
C10G 1/002 (2013.01); C07C 4/04 (2013.01); C08F 10/02 (2013.01); C10B 53/07 (2013.01); C10B 57/06 (2013.01); C10G 1/10 (2013.01); C10G 9/36 (2013.01); C10G 11/18 (2013.01); C10L 1/06 (2013.01); C10L 1/08 (2013.01); C10L 3/06 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/4081 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/20 (2013.01); C10G 2400/26 (2013.01); C10G 2400/30 (2013.01); C10L 2200/0461 (2013.01); C10L 2270/023 (2013.01); C10L 2270/026 (2013.01);
Abstract

Processes for using pyrolysis gas as a feedstock or a co-feedstock for making a variety of chemicals, for example, circular ethylene, circular ethylene polymers and copolymers, and other circular products. In these processes, pyrolysis reactor conditions can be selected to increase or optimized the production of pyrolysis gas over pyrolysis oil, and the pyrolysis gas which is usually used as fuel or flared can be fed downstream of the steam cracker furnace for economic use to form circular chemicals. Operating parameters of the pyrolysis unit may be adjusted to increase or decrease the proportion of pyrolysis gas relative to pyrolysis liquid as a function of their relative economic values.


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