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:
Jun. 04, 2019

Filed:

Dec. 16, 2016
Applicant:

Johnson Matthey Davy Techhnologies Limited, London, GB;

Inventor:

Kar Chi Yiu, London, GB;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 3/14 (2006.01); C01B 3/50 (2006.01); B01J 23/72 (2006.01); C07C 31/04 (2006.01); C07C 29/151 (2006.01); C07C 29/152 (2006.01); C07C 29/154 (2006.01);
U.S. Cl.
CPC ...
C07C 29/1516 (2013.01); B01D 3/143 (2013.01); B01J 23/72 (2013.01); C01B 3/506 (2013.01); C07C 29/152 (2013.01); C07C 29/154 (2013.01); C07C 31/04 (2013.01); B01D 2256/16 (2013.01); B01D 2257/70 (2013.01); B01J 2203/06 (2013.01); B01J 2523/17 (2013.01); B01J 2523/27 (2013.01); B01J 2523/31 (2013.01); C01B 2203/0216 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/061 (2013.01); Y02P 20/132 (2015.11);
Abstract

A process is described for the synthesis of methanol comprising the steps of: (i) passing a first synthesis gas mixture comprising a make-up gas through a first synthesis reactor containing a cooled methanol synthesis catalyst to form a first product gas stream, (ii) recovering methanol from the first product gas stream thereby forming a first methanol-depleted gas mixture, (iii) combining the first methanol-depleted gas mixture with a loop recycle gas stream to form a second synthesis gas mixture, (iv) passing the second synthesis gas mixture through a second synthesis reactor containing a cooled methanol synthesis catalyst to form a second product gas stream, (v) recovering methanol from the second product gas stream thereby forming a second methanol-depleted gas mixture, and (vi) using at least part of the second methanol-depleted gas mixture as the loop recycle gas stream, wherein the first synthesis reactor has a higher heat transfer per cubic meter of catalyst than the second synthesis reactor, none of the loop recycle gas stream is fed to the first synthesis gas mixture and the recycle ratio of the loop recycle gas stream to form the second synthesis gas mixture is in the range 1.1:1 to 6:1.


Find Patent Forward Citations

Loading…