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:
Jan. 21, 2020

Filed:

Feb. 26, 2016
Applicant:

Johnson Matthey Davy Technologies Limited, London, GB;

Inventors:

John Swinney, Durham, GB;

Simon Nicholas Tilley, Durham, GB;

David J. Watson, Durham, GB;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/22 (2006.01); B01D 53/86 (2006.01); B01D 53/90 (2006.01); C10L 3/10 (2006.01);
U.S. Cl.
CPC ...
B01D 53/229 (2013.01); B01D 53/864 (2013.01); B01D 53/8696 (2013.01); B01D 53/90 (2013.01); C10L 3/104 (2013.01); B01D 53/225 (2013.01); B01D 2251/11 (2013.01); B01D 2251/208 (2013.01); B01D 2255/1021 (2013.01); B01D 2255/1023 (2013.01); B01D 2255/1028 (2013.01); B01D 2256/22 (2013.01); B01D 2256/245 (2013.01); B01D 2257/504 (2013.01); B01D 2257/7025 (2013.01);
Abstract

A method for treating a crude natural gas feed stream comprising methane and having a first carbon dioxide concentration, said method comprising the steps of: subjecting the crude natural gas feed stream to a separation process to provide: a purified natural gas stream having a second carbon dioxide content which is lower than the first carbon dioxide concentration in said crude natural gas stream; and, a carbon dioxide stream comprising carbon dioxide as the major component and methane; recovering the purified natural gas steam; optionally mixing the carbon dioxide stream with make-up methane and/or make-up air; passing the carbon dioxide stream and optional make-up methane or air through a heat exchanger to raise the temperature of the stream to the desired inlet temperature Tof an oxidation reactor; optionally mixing the carbon dioxide stream with make-up methane and/or make-up air; passing the heated stream from step (d) and any optional make-up methane and/or air to the oxidation reactor containing an oxidation catalyst, where the methane is oxidised; removing a gas stream including the products of the oxidation reaction from the reactor, said gas stream being at an outlet temperature Twhich is higher than the inlet temperature T; passing the gas stream removed in step (g) through the heat exchanger against the carbon dioxide stream from step (a) to allow the heat to be recovered from the gas stream removed in step (g) and utilised to heat the carbon dioxide stream in step (d); and measuring the outlet temperature Tand controlling the inlet temperature Tby adjusting the amount of make-up methane and/or air added in step (c) and/or step (e).


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