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. 14, 2023

Filed:

Oct. 16, 2020
Applicant:

Conocophillips Company, Houston, TX (US);

Inventors:

Jinghua Chan, Houston, TX (US);

Qi Ma, Houston, TX (US);

Dale L. Embry, Houston, TX (US);

Attilio J. Praderio, Houston, TX (US);

Assignee:

ConocoPhillips Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/02 (2006.01); F25J 1/00 (2006.01); F25J 1/02 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0022 (2013.01); F25J 1/004 (2013.01); F25J 1/0247 (2013.01); F25J 3/0209 (2013.01); F25J 3/0233 (2013.01); F25J 3/0242 (2013.01); F25J 3/0295 (2013.01); F25J 2200/02 (2013.01); F25J 2200/76 (2013.01); F25J 2200/78 (2013.01); F25J 2205/02 (2013.01); F25J 2220/60 (2013.01); F25J 2220/64 (2013.01); F25J 2245/02 (2013.01); F25J 2270/12 (2013.01); F25J 2270/60 (2013.01);
Abstract

Implementations described and claimed herein provide systems and methods for processing liquefied natural gas (LNG). In one implementation, a dry feed gas is received. The dry feed gas is chilled with clean vapor from a heavies removal column to form a chilled feed gas. The chilled feed gas is partially condensed into a vapor phase and a liquid phase. The liquid phase retains freezing components. The freezing components are extracted using a reflux stream in the heavies removal column. The freezing components are removed as a condensate. The vapor phase is compressed into a clean feed gas. The clean feed gas is free of the freezing components for downstream liquefaction.


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