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:
Sep. 06, 2016

Filed:

Mar. 13, 2012
Applicants:

Yasuhiro Onishi, Tokyo, JP;

Kazuhiko Tasaka, Yokohama, JP;

Tomoyuki Mikuriya, Kawasaki, JP;

Inventors:

Yasuhiro Onishi, Tokyo, JP;

Kazuhiko Tasaka, Yokohama, JP;

Tomoyuki Mikuriya, Kawasaki, JP;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/00 (2006.01); C07C 1/02 (2006.01); C07C 1/04 (2006.01); C10G 2/00 (2006.01); B01J 8/00 (2006.01); B01J 8/18 (2006.01); B01J 8/20 (2006.01); B01J 8/22 (2006.01); B01J 19/00 (2006.01); B01J 19/24 (2006.01);
U.S. Cl.
CPC ...
C07C 1/041 (2013.01); B01J 8/1809 (2013.01); B01J 8/22 (2013.01); B01J 19/0013 (2013.01); B01J 19/0033 (2013.01); C10G 2/342 (2013.01); B01J 2208/00061 (2013.01); B01J 2208/00274 (2013.01); B01J 2208/00548 (2013.01); B01J 2208/00646 (2013.01); B01J 2219/00202 (2013.01); B01J 2219/00213 (2013.01); B01J 2219/00231 (2013.01); B01J 2219/00238 (2013.01); C10G 2300/4031 (2013.01); C10G 2300/4081 (2013.01);
Abstract

The hydrocarbon synthesis reaction apparatus is provided with a synthesis gas supply line in which a synthesis gas is compressed and supplied by a first compressor, a reactor configured to accommodate a catalyst slurry, a gas-liquid separator configured to separate an unreacted synthesis gas and hydrocarbons discharged from the reactor into a gas and a liquid, a first recycle line in which the unreacted synthesis gas after separation into a gas and a liquid is compressed and recycled into the reactor by a second compressor, and a second recycle line configured to recycle a residual unreacted synthesis gas after separation into a gas and a liquid into the inlet side of the first compressor at the time of start-up operation when the synthesis gas is gradually increased in the amount to be introduced.


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