Process and plant for separating a gas mixture

Patent metadata

Field	Value
Publication number	US-10066870-B2
Application number	US-201615271633-A
Country	US
Kind code	B2
Filing date	Sep 21, 2016
Priority date	Sep 23, 2015
Publication date	Sep 4, 2018
Grant date	Sep 4, 2018

Abstract

A process and plant are proposed for separating a feed mixture predominantly or exclusively containing carbon monoxide and hydrogen, in which the feed mixture is subjected to a cryogenic separation process in which a carbon monoxide-rich liquid and at least one residual gas mixture which is depleted in carbon monoxide and enriched in hydrogen, in comparison with the feed mixture, are formed. It is intended that the at least one residual gas mixture is subjected to a membrane separation process in which at least one hydrogen-rich permeate and at least one carbon monoxide-rich retentate are formed, wherein the or at least one of the carbon monoxide-rich retentates is recirculated to the cryogenic separation process.

First claim

What I claim is:

1. A process for separating a feed mixture predominantly or exclusively containing carbon monoxide and hydrogen, in which the feed mixture is subjected to a cryogenic separation process in which a carbon monoxide-rich liquid and at least one residual gas mixture which is depleted in carbon monoxide and enriched in hydrogen, in comparison with the feed mixture, are formed, characterized in that the at least one residual gas mixture is subjected to a membrane separation process comprising a first membrane separation step and a second membrane separation step, wherein in the first membrane separation step a first hydrogen-rich permeate and a first carbon monoxide-rich retentate are formed, and in the second membrane separation step, a second hydrogen-rich permeate and a second carbon monoxide-rich retentate are formed wherein the first carbon monoxide-rich retentate or the second carbon monoxide-rich retentate is recirculated to the cryogenic separation process, wherein the first hydrogen-rich permeate is transferred from the first membrane separation step, to the second membrane separation step and the first membrane separation step is carried out at a first pressure level at the height of the pressure level of the feed mixture and the second membrane separation step is carried out at a second pressure level below the first pressure level.

2. The process according to claim 1 , in which, in the cryogenic separation process, a first residual gas mixture and a second residual gas mixture are formed, wherein the first residual gas mixture is fed to the first membrane separation step and the second residual gas mixture is fed to the second membrane separation step.

3. The process according to claim 2 , in which the first residual gas mixture has a higher carbon monoxide content than the second residual gas mixture, and the first hydrogen-rich permeate has a higher carbon monoxide content than the second hydrogen-rich permeate.

4. The process according to claim 2 , in which, in the cryogenic separation process, first by partial condensation of the feed mixture to the first pressure level in a separation container, with the first residual gas mixture remaining, a liquid intermediate fraction is formed.

5. The process according to claim 4 , in which the liquid intermediate fraction in the cryogenic separation process is expanded to an intermediate pressure level and is fed into a stripping column from which the second residual gas mixture and the carbon monoxide-rich liquid are withdrawn, wherein the intermediate pressure level is selected from the group consisting of a pressure level between the first and second pressure levels and the second pressure level.

6. The process according to claim 5 , in which the second residual gas mixture after the withdrawal from the stripping column is expanded to the second pressure level before being fed to the second membrane separation step.

7. The process according to claim 2 , in which the first residual gas mixture and the second residual gas mixtures are warmed in counterflow to the feed mixture.

8. The process according to claim 5 , in which the first and second carbon monoxide-rich retentates are brought to the intermediate pressure level, combined and fed into the stripping column.

9. The process according to claim 5 , in which the first carbon monoxide-rich retentate is expanded to the intermediate pressure level and fed into the stripping column and the second carbon monoxide-rich retentate is elevated in pressure to the first pressure level and combined with the fed mixture.

10. The process according to claim 2 , in which the first and second carbon monoxide-rich retentates are increased in pressure to the first pressure level and combined with the feed mixture.

11. The process according to claim 10 , in which a shared compression process is used for the pressure elevation of the first and second carbon monoxide-rich retentates to the first pressure level.

Assignees

• Klein Bernd
• Linde Ag

Inventors

• Klein Bernd

Classifications

• F25J3/0271

  separation of H2/CO mixtures, i.e. of synthesis gas (production of carbon monoxide containing gas in general C01B32/40, C10J, C10K, production of hydrogen containing gas C01B3/00) · CPC title

• F25J2215/02

  Mixing or blending of fluids to yield a certain product · CPC title

• C01B3/501

  by diffusion · CPC title

• F25J2205/04

  in the feed line, i.e. upstream of the fractionation step · CPC title

• F25J2205/80

  using membrane, i.e. including a permeation step · CPC title