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:
Oct. 27, 2020

Filed:

Mar. 10, 2016
Applicant:

Jgc Corporation, Yokohama, JP;

Inventors:

Yoshiyuki Watanabe, Kanagawa, JP;

Hidefumi Omori, Kanagawa, JP;

Toru Matsuhara, Kanagawa, JP;

Shintaro Watanabe, Kanagawa, JP;

Toru Nakayama, Kanagawa, JP;

Assignee:

JGC CORPORATION, Yokohama, JP;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 1/02 (2006.01); F25J 1/00 (2006.01); C01B 3/38 (2006.01); F25B 9/00 (2006.01); C01B 3/50 (2006.01);
U.S. Cl.
CPC ...
F25J 1/001 (2013.01); C01B 3/38 (2013.01); C01B 3/506 (2013.01); F25B 9/00 (2013.01); F25J 1/004 (2013.01); F25J 1/005 (2013.01); F25J 1/0022 (2013.01); F25J 1/0052 (2013.01); F25J 1/0065 (2013.01); F25J 1/0067 (2013.01); F25J 1/0072 (2013.01); F25J 1/0087 (2013.01); F25J 1/021 (2013.01); F25J 1/0211 (2013.01); F25J 1/0217 (2013.01); F25J 1/0229 (2013.01); F25J 1/0236 (2013.01); C01B 2203/0227 (2013.01); C01B 2203/043 (2013.01); C01B 2203/046 (2013.01); C01B 2203/048 (2013.01); C01B 2203/0415 (2013.01); C01B 2203/0495 (2013.01); C01B 2203/127 (2013.01); F25J 2210/60 (2013.01); F25J 2215/10 (2013.01); F25J 2220/02 (2013.01); F25J 2220/60 (2013.01); F25J 2220/66 (2013.01); F25J 2260/60 (2013.01); F25J 2260/80 (2013.01); F25J 2270/16 (2013.01);
Abstract

Provided is a production facility for liquefied hydrogen and a liquefied natural gas from a natural gas, including: a first heat exchanger configured to cool a hydrogen gas through heat exchange between the hydrogen gas and a mixed refrigerant for liquefying a natural gas containing a plurality of kinds of refrigerants selected from the group consisting of methane, ethane, propane, and nitrogen; a second heat exchanger configured to cool the mixed refrigerant through heat exchange between the mixed refrigerant and propane; and a third heat exchanger configured to cool the hydrogen gas through heat exchange between the hydrogen gas and a refrigerant containing hydrogen or helium, wherein the first heat exchanger has a precooling temperature of from −100° C. to −160° C.


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