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:
Aug. 30, 2016

Filed:

Dec. 02, 2015
Applicant:

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

Inventors:

Lei Ji, Kingwood, TX (US);

Ai-Fu Chang, Humble, TX (US);

Assignee:

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

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/047 (2006.01); C07C 7/12 (2006.01); C07C 7/13 (2006.01); C08F 10/02 (2006.01); C07C 7/00 (2006.01); C07C 7/04 (2006.01); B01J 8/20 (2006.01); B01J 19/24 (2006.01); C08F 2/14 (2006.01); B01J 19/18 (2006.01);
U.S. Cl.
CPC ...
B01D 53/047 (2013.01); B01J 8/20 (2013.01); B01J 19/245 (2013.01); B01J 19/2435 (2013.01); C07C 7/005 (2013.01); C07C 7/04 (2013.01); C07C 7/12 (2013.01); C07C 7/13 (2013.01); C08F 10/02 (2013.01); B01D 2253/108 (2013.01); B01D 2256/24 (2013.01); B01D 2257/702 (2013.01); B01D 2259/402 (2013.01); B01D 2259/40086 (2013.01); B01J 2208/00265 (2013.01); B01J 2219/00105 (2013.01); Y02P 20/582 (2015.11);
Abstract

A process for component separation in a polymer production system comprising: (a) separating a polymerization product into a gas stream and a polymer stream; (b) processing the gas stream in distillation columns to yield a light hydrocarbon stream (LHS) comprising ethylene and ethane; (c) contacting LHS with a purged hydrocarbon adsorber to yield a loaded hydrocarbon adsorber and a non-adsorbed gas stream, wherein ethane is adsorbed by the purged hydrocarbon adsorber at a first pressure to yield adsorbed ethane, and wherein the non-adsorbed gas stream comprises recovered ethylene; (d) contacting the loaded hydrocarbon adsorber with a sweeping gas stream at a second pressure to yield an unloaded hydrocarbon adsorber and a recovered adsorbed gas stream comprising the sweeping gas stream and desorbed ethane; and (e) contacting the unloaded hydrocarbon adsorber with the sweeping gas stream at the first pressure to yield the purged hydrocarbon adsorber and a spent sweeping gas.


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