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. 17, 2015

Filed:

Jun. 15, 2009
Applicants:

Peter John Herbert Carnell, Stockton on Tees, GB;

Ginny Yuen Che NG, East Perth, AU;

Inventors:

Peter John Herbert Carnell, Stockton on Tees, GB;

Ginny Yuen Che Ng, East Perth, AU;

Assignee:

Johnson Matthey PLC, London, GB;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10J 3/46 (2006.01); C01B 3/24 (2006.01); F25J 3/00 (2006.01); C07C 27/06 (2006.01); F25J 1/00 (2006.01); C01B 3/38 (2006.01); C10L 3/08 (2006.01); C10L 3/10 (2006.01); F25J 1/02 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0022 (2013.01); C01B 3/38 (2013.01); C10L 3/08 (2013.01); C10L 3/102 (2013.01); F25J 1/0229 (2013.01); F25J 1/0278 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0405 (2013.01); C01B 2203/0415 (2013.01); C01B 2203/042 (2013.01); C01B 2203/0445 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/0495 (2013.01); C01B 2203/1052 (2013.01); C01B 2203/1058 (2013.01); C01B 2203/1064 (2013.01); C01B 2203/1247 (2013.01); C01B 2203/1252 (2013.01); C01B 2203/1258 (2013.01); C01B 2203/127 (2013.01); C01B 2203/1288 (2013.01); C01B 2203/1294 (2013.01); C01B 2203/146 (2013.01); C01B 2203/148 (2013.01); F25J 2210/06 (2013.01); F25J 2220/64 (2013.01);
Abstract

A process for treating offshore natural gas includes processing the natural gas on an off-shore processing facility by, (i) liquefying and fractionating the natural gas to generate a liquefied natural gas stream and a higher hydrocarbon stream, (ii) vaporizing at least a portion of the higher hydrocarbon stream, (iii) passing the vaporized higher hydrocarbon stream and steam over a steam reforming catalyst to generate a reformed gas mixture comprising methane, steam, carbon oxides and hydrogen, (iv) passing the reformed gas mixture over a methanation catalyst to generate a methane rich gas, and (v) combining the methane-rich gas with the natural gas prior to the liquefaction step.


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