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. 03, 2017

Filed:

Jun. 22, 2012
Applicants:

Marc Bonnissel, Montigny le Bretonneux, FR;

Bertrand Du Parc, Voisins le Bretonneux, FR;

Eric Zielinski, Versailles, FR;

Inventors:

Marc Bonnissel, Montigny le Bretonneux, FR;

Bertrand Du Parc, Voisins le Bretonneux, FR;

Eric Zielinski, Versailles, FR;

Assignee:

Saipem S.A., Montigny le Bretonneux, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 1/00 (2006.01); F25B 9/06 (2006.01); F25J 1/02 (2006.01); C09K 5/04 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0022 (2013.01); C09K 5/041 (2013.01); C09K 5/042 (2013.01); F25B 9/06 (2013.01); F25J 1/005 (2013.01); F25J 1/0072 (2013.01); F25J 1/0097 (2013.01); F25J 1/0204 (2013.01); F25J 1/0212 (2013.01); F25J 1/0254 (2013.01); F25J 1/0283 (2013.01); F25J 1/0287 (2013.01); F25J 1/0288 (2013.01); C09K 2205/13 (2013.01); C09K 2205/132 (2013.01); F25J 2270/16 (2013.01);
Abstract

A method for liquefying a natural gas primarily including methane, preferably at least 85% of methane, the other components essentially including nitrogen and C2-C4 alkanes, in which the natural gas to be liquefied is liquefied by circulating at a pressure P0 no lower than the atmospheric pressure (Patm), P0 preferably being higher than the atmospheric pressure, in at least one cryogenic heat-exchanger (EC, EC, EC) by a counter-current closed-circuit circulation in indirect contact with at least one stream of coolant gas remaining in the compressed gaseous state at a pressure P1 that is entering the cryogenic heat-exchanger at a temperature T3' that is lower than T3, T3 being the liquefaction temperature of the liquefied natural gas at the pressure P0 at the output of said cryogenic exchanger, characterized in that the coolant gas includes a mixture of nitrogen and at least one other component selected from among neon and hydrogen.


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