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:
Feb. 26, 2019

Filed:

Feb. 11, 2016
Applicant:

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

Inventors:

Vincent White, Ashtead, GB;

Paul Higginbotham, Surrey, GB;

John Eugene Palamara, Macungie, PA (US);

Alan Berger, North Wales, PA (US);

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);
U.S. Cl.
CPC ...
F25J 3/0209 (2013.01); F25J 3/029 (2013.01); F25J 3/0233 (2013.01); F25J 3/0238 (2013.01); F25J 3/0257 (2013.01); F25J 3/08 (2013.01); F25J 2200/02 (2013.01); F25J 2200/04 (2013.01); F25J 2200/08 (2013.01); F25J 2200/10 (2013.01); F25J 2200/40 (2013.01); F25J 2200/50 (2013.01); F25J 2200/70 (2013.01); F25J 2200/72 (2013.01); F25J 2200/74 (2013.01); F25J 2205/02 (2013.01); F25J 2205/04 (2013.01); F25J 2205/40 (2013.01); F25J 2205/60 (2013.01); F25J 2205/64 (2013.01); F25J 2210/06 (2013.01); F25J 2210/60 (2013.01); F25J 2215/04 (2013.01); F25J 2220/02 (2013.01); F25J 2220/66 (2013.01); F25J 2220/68 (2013.01); F25J 2235/42 (2013.01); F25J 2235/60 (2013.01); F25J 2240/02 (2013.01); F25J 2240/40 (2013.01); F25J 2245/02 (2013.01); F25J 2250/20 (2013.01); F25J 2260/20 (2013.01); F25J 2260/44 (2013.01); F25J 2270/02 (2013.01); F25J 2270/04 (2013.01); F25J 2290/34 (2013.01);
Abstract

Helium can be recovered from nitrogen-rich natural gas at high pressure with low helium loss by cryogenic distillation of the natural gas after pre-treatment of the gas to remove incompatible impurities and then recovery of natural gas liquid (NGL) from the pre-treated gas by distillation. Overall power consumption may be reduced, particularly if the feed to the helium recovery column system is at least substantially condensed by indirect heat exchange against a first portion of nitrogen-enriched bottoms liquid at first pressure, and a second portion of nitrogen-enriched bottoms liquid at a second pressure that is different from the first pressure.


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