IP Library Granted Patent US 10,335,734
Granted Patent B2
US 10,335,734 · App. 15/270,410 · Granted Jul 2, 2019

Gas separation process

Inventors: Davide Bocciardo (Tilburg, NL); Yujiro Itami (Tilburg, NL)
Assignees: Fujifilm Manufacturing Europe B.V.; Fujifilm Corporation
B01D53/226B01D63/12B01D71/32B01D71/64B01D53/228B01D2256/245B01D2257/304B01D2257/504B01D2317/022B01D2317/08B01D2319/022B01D2319/06Y02C10/10
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Quick Facts
Patent No.
US 10,335,734
App. No.
15/270,410
Granted
Jul 2, 2019
Kind
B2
Abstract

A process for separating a feed gas comprising polar and non-polar gases into a gas mixture enriched in polar gas(es) and a gas mixture depleted in polar gas(es), the process comprising passing the feed gas through a gas separation unit comprising at least two gas-separation modules in order of decreasing selectivity for the polar gas(es), wherein the feed gas entering the gas separation unit comprises 1 to 35 mol % of polar gas(es).

Claims (16)

1. A process for separating a feed gas comprising CO 2 and non-polar gases into a gas mixture enriched in CO 2 and a gas mixture depleted in CO 2 , the process comprising passing the feed gas through a gas separation unit comprising at least two gas-separation modules in order of decreasing selectivity for the CO 2 , wherein (i) the feed gas entering the gas separation unit comprises 1 to 35 mol % of CO 2 ; (ii) each gas-separation module comprises a gas separation membrane; (iii) the feed gas is passed through a first set of gas-separation modules and then through a second set of gas-separation modules, wherein each of the gas-separation modules in the second set of gas-separation modules has a lower CO 2 selectivity than all of the gas-separation modules in the first set of gas-separation modules; and (iv) all of the gas-separation modules in the second set of gas-separation modules comprise gas separation membranes having an αCO 2 /CH 4 selectivity of 5 to 25 and all of the gas-separation modules in the first set of gas-separation modules comprise gas separation membranes having an αCO 2 /CH 4 selectivity of 20 to 50.

2. The process according to claim 1 wherein the second set of gas-separation modules comprises at least three gas-separation modules.

3. The process according to claim 1 wherein the gas-separation modules of the first set of gas-separation modules have identical CO 2 selectivity to each other.

4. The process according to claim 1 wherein the gas-separation modules of the second set of gas-separation modules have identical CO 2 selectivity to each other.

5. The process according to claim 1 wherein the feed gas enters a first gas-separation module of the at least two gas-separation modules at a temperature below 60° C.

6. The process according to claim 1 wherein the gas-separation modules are spiral wound gas-separation modules.

7. The process according to claim 1 wherein the gas separation unit further comprises a housing which contains the gas separation modules, the gas separation modules are connected in series and wherein the housing further comprises a gas inlet and at least two gas outlets.

8. The process according to claim 7 wherein the gas separation unit is free from temperature controlling devices and gas pressure controlling devices.

9. The process according to claim 1 wherein the gas-separation modules comprise gas separation membranes having polyimide discriminating layers comprising —CF 3 groups and optionally carboxylic acid groups.

10. The process according to claim 1 wherein the feed gas is fed into a first of the at least two gas-separation modules at a pressure of 20 to 60 bar.

11. The process according to claim 1 wherein the feed gas is fed into a first of the at least two gas-separation modules at a flow rate of 0.5 to 1.5 MMSCFD.

12. The process according to claim 1 wherein the feed gas is fed into a first of the at least two gas-separation modules at a temperature of 30 to 50° C.

13. The process according to claim 1 wherein the gas separation unit comprises a series of modules not all of which have the same CO 2 selectivity, each module comprising the gas separation membrane which separates gas into a permeate which passes through the gas separation membrane and a retentate which does not pass through that membrane, wherein gas flows through the gas separation unit such that retentate from each module except for a final module becomes the feed gas for a next module and wherein the gas-separation modules are arranged such that the CO 2 selectivity of a first module through which the gas flows is higher than the CO 2 selectivity of the final module through which the gas flows.

14. The process according to claim 13 wherein the series of modules comprises a first set of gas-separation modules and a second set of gas-separation modules, wherein each of the gas-separation modules in the second set of gas-separation modules has a lower CO 2 selectivity than all of the gas-separation modules in the first set of gas-separation modules and wherein the gas separation unit and the gas-separation modules are arranged such that the retentate from each module except for the final module is the feed gas for the next module.

15. The process according to claim 1 wherein the non-polar gas(es) are or comprise CH 4 .

16. The process according to claim 13 wherein the non-polar gas(es) are or comprise CH 4 .

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 17, 2026
From: YESTAR ADVANCED MATERIALS (HK) CO., LIMITED
To: YESTAR ADVANCED MATERIALS (SUZHOU) CO., LTD.
Reel/Frame 076045/0973 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2026
From: FUJIFILM CORPORATION; FUJIFILM MANUFACTURING EUROPE B.V.
To: YESTAR ADVANCED MATERIALS (HK) CO., LIMITED
Reel/Frame 075440/0524 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 19, 2017
From: BOCCIARDO, DAVIDE; ITAMI, YUJIRO
To: FUJIFILM MANUFACTURING EUROPE B.V.; FUJIFILM CORPORATION
Reel/Frame 041017/0910 →
Continuity (2)
Provisional Application 62221372 · Sep 21, 2015
Related Publication 20170080381A1 · Mar 23, 2017