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:
Dec. 15, 2015

Filed:

Jan. 21, 2011
Applicants:

Michael Edward Bailey, Colchester, GB;

Stefano Consonni, Piacenza, IT;

Jonathan Alec Forsyth, Newbury, GB;

Manuele Gatti, Ripalta Cremasca, IT;

Emanuele Martelli, Piacenza, IT;

Yasushi Mori, Hiroshima, JP;

Kazumasa Ogura, Tokyo, JP;

Federico Vigano, Piacenza, IT;

Inventors:

Michael Edward Bailey, Colchester, GB;

Stefano Consonni, Piacenza, IT;

Jonathan Alec Forsyth, Newbury, GB;

Manuele Gatti, Ripalta Cremasca, IT;

Emanuele Martelli, Piacenza, IT;

Yasushi Mori, Hiroshima, JP;

Kazumasa Ogura, Tokyo, JP;

Federico Vigano, Piacenza, IT;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/00 (2006.01); C01B 3/50 (2006.01); C01B 3/52 (2006.01); F25J 3/06 (2006.01);
U.S. Cl.
CPC ...
C01B 3/506 (2013.01); C01B 3/52 (2013.01); F25J 3/067 (2013.01); F25J 3/0625 (2013.01); F25J 3/0655 (2013.01); C01B 2203/046 (2013.01); C01B 2203/0415 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/0485 (2013.01); C01B 2203/0805 (2013.01); C01B 2203/0883 (2013.01); C01B 2203/146 (2013.01); F25J 2205/40 (2013.01); F25J 2205/50 (2013.01); F25J 2215/04 (2013.01); F25J 2230/30 (2013.01); F25J 2240/30 (2013.01); F25J 2270/06 (2013.01); Y02C 10/12 (2013.01);
Abstract

A process for separating sour shifted synthesis gas feedstock into liquid carbon dioxide, a gaseous hydrogen-containing gas and separated sulphur-containing components includes the steps of a. scrubbing the sour shifted gas elevated pressure with an alcohol solvent in a first scrubber and separately recovering an alcohol stream containing the sulphur-containing components and a sweet shifted gas; b. thereafter cooling the sweet shifted gas to a temperature and elevated pressure at which the carbon dioxide contained therein condenses and a two-phase gas-liquid mixture is formed; c. separating the two-phase mixture of stage (b) into separate liquid carbon dioxide and gaseous hydrogen-containing fractions in a fractionation unit; d. extracting residual carbon dioxide from the separated gaseous hydrogen-containing fraction by scrubbing the gaseous hydrogen-containing fraction at elevated pressure with an alcohol solvent in a second scrubber and recovering an alcohol stream containing carbon dioxide; e. feeding the alcohol stream containing carbon dioxide produced in step (d) to the first scrubber and f. warming and expanding the scrubber gaseous hydrogen-containing fraction using at least one heat exchanger to exchange heat with the mixture of step (b) and at least one turbo-expander capable of recovering mechanical work. The process described may be used in for example Integrated Gasification Combined Cycles (IGCC) where the source of fuel is coal or low grade carbon sources such as lignite, tar sands and shale oil.


Find Patent Forward Citations

Loading…