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. 23, 2019

Filed:

Dec. 30, 2013
Applicant:

Air Products and Chemicals, Inc., Allentown, PA (US);

Inventors:

Paul Higginbotham, Surrey, GB;

Liu Yang, Yorba Linda, CA (US);

John Eugene Palamara, Macungie, PA (US);

Vincent White, Ashtead, GB;

Assignee:

Air Products and Chemicals, Inc., Allentown, PA (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/00 (2006.01); F25J 3/02 (2006.01); F25J 3/08 (2006.01); E21B 43/16 (2006.01); E21B 43/40 (2006.01); C10G 70/04 (2006.01); C10G 7/00 (2006.01); B01D 3/14 (2006.01); C10G 5/06 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0242 (2013.01); B01D 3/143 (2013.01); C10G 7/00 (2013.01); C10G 70/041 (2013.01); E21B 43/164 (2013.01); E21B 43/40 (2013.01); F25J 3/0209 (2013.01); F25J 3/0266 (2013.01); F25J 3/08 (2013.01); C10G 5/06 (2013.01); F25J 2200/02 (2013.01); F25J 2200/04 (2013.01); F25J 2200/30 (2013.01); F25J 2200/50 (2013.01); F25J 2200/72 (2013.01); F25J 2200/74 (2013.01); F25J 2200/76 (2013.01); F25J 2205/50 (2013.01); F25J 2215/02 (2013.01); F25J 2220/84 (2013.01); F25J 2260/60 (2013.01); F25J 2260/80 (2013.01); F25J 2270/12 (2013.01); F25J 2270/60 (2013.01); F25J 2270/88 (2013.01); Y02C 10/12 (2013.01); Y02P 90/70 (2015.11);
Abstract

The power required to recover Chydrocarbons from crude carbon dioxide comprising Chydrocarbons and hydrogen sulfide may be reduced by distilling the crude carbon dioxide to produce carbon dioxide-enriched overhead vapor and Chydrocarbon-enriched bottoms liquid such that the hydrogen sulfide is rejected with the overhead vapor. Power consumption reductions may be achieved by incorporating a heat pump cycle using carbon dioxide vapor as working fluid to provide at least a part of the refrigeration duty and using a side reboiler to reduce the bottom reboiler duty. Where the bottoms liquid is further processed to produce 'lighter' and 'heavier' hydrocarbon fractions, the process enables optimization of upgrading crude oil on the basis of API gravity, Reid Vapor pressure and/or viscosity.


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