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:
Mar. 12, 2024

Filed:

Jan. 10, 2022
Applicant:

Exxonmobil Technology and Engineering Company, Spring, TX (US);

Inventors:

Robert D. Kaminsky, Houston, TX (US);

Marcel Staedter, Houston, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
F25J 1/00 (2006.01); F25J 1/02 (2006.01); F25J 3/02 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0022 (2013.01); F25J 1/0032 (2013.01); F25J 1/005 (2013.01); F25J 1/007 (2013.01); F25J 1/008 (2013.01); F25J 1/0254 (2013.01); F25J 3/0214 (2013.01); F25J 2210/06 (2013.01); F25J 2210/60 (2013.01); F25J 2215/04 (2013.01); F25J 2220/66 (2013.01); F25J 2260/02 (2013.01); F25J 2270/04 (2013.01); F25J 2270/14 (2013.01);
Abstract

A method and apparatus for liquefying a feed gas stream comprising natural gas and carbon dioxide. A method includes compressing an input fluid stream to generate a first intermediary fluid stream; cooling the first intermediary fluid stream with a first heat exchanger to generate a second intermediary fluid stream, wherein a temperature of the second intermediary fluid stream is higher than a carbon dioxide-freezing temperature for the second intermediary fluid stream; expanding the second intermediary fluid stream to generate a third intermediary fluid stream, wherein the third intermediary fluid stream comprises solid carbon dioxide; separating the third intermediary fluid stream into a fourth intermediary fluid stream and an output fluid stream, wherein the output fluid stream comprises a liquefied natural gas (LNG) liquid; and utilizing the fourth intermediary fluid stream as a cooling fluid stream for the first heat exchanger.


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