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. 28, 2020

Filed:

Dec. 20, 2012
Applicants:

1304342 Alberta Ltd, Edmonton, CA;

1304338 Alberta Ltd, Edmonton, CA;

Inventors:

Jose Lourenco, Edmonton, CA;

MacKenzie Millar, Edmonton, CA;

Assignees:

1304338 Alberta Ltd, Edmonton, CA;

1304342 Alberta Ltd, Edmonton, CA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/02 (2006.01); F25J 1/00 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0022 (2013.01); F25J 3/0209 (2013.01); F25J 3/0233 (2013.01); F25J 3/0238 (2013.01); F25J 2200/02 (2013.01); F25J 2200/74 (2013.01); F25J 2205/04 (2013.01); F25J 2215/04 (2013.01); F25J 2220/04 (2013.01); F25J 2220/66 (2013.01); F25J 2240/02 (2013.01); F25J 2245/02 (2013.01); F25J 2270/02 (2013.01); F25J 2270/04 (2013.01); F25J 2280/02 (2013.01);
Abstract

A method for production of liquid natural gas (LNG) at natural gas liquids (NGLs) recovery plants that maximizes NGLs recovery by producing LNG and using the produced LNG as an external cooling source to control the operation of a de-methanizer column at the NLG recovery facility. In at least one embodiment, LNG is added from an LNG overhead receiver by direct mixing to control the temperature profile in the NGL de-methanizer column. The temperature in an overhead product of the de-methanizer column is controlled by controlling addition of LNG as a reflux stream. The temperature in an expanded feed gas to the de-methanizer column is controlled by controlling addition of LNG as a tempering gas, while stripping of carbon dioxide from an NGL product stream is controlled by controlling the addition of LNG as stripping gas.


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