Granted Patent B2

US 12,345,470 · App. 18/266,072 · Granted Jul 1, 2025

Inventors: Uwe Jordan (Worpswede, DE); Gamuret Hack (Zürich, CH); Lukas Völlmy (Winterthur, CH)

Assignee: HITACHI ZOSEN INOVA AG

F25J3/0635B01D53/0462B01D53/047F25J3/067B01D2256/245B01D2257/504B01D2259/40052F25J2205/40F25J2205/64F25J2245/02

Abstract

Claims (21)

1. A process for obtaining a methane-enriched product gas from a methane-containing gas comprising the steps of:

a) providing a methane-containing gas containing at least CO 2 as an impurity and cooling the methane-containing gas in a first heat exchanger;

b) further cooling the methane-containing gas of step a) to remove CO 2 from the methane-containing gas from step a) by freezing-out;

c) further reducing the CO 2 concentration of the methane-containing gas from step b) using a pressure temperature swing adsorption apparatus (PTSA) to obtain a methane-enriched product gas;

d) using at least a portion of the methane-enriched product gas from step c) as treatment gas which is passed through the PTSA for treatment of the PTSA, whereby CO 2 is absorbed by the treatment gas and removed from the PTSA as a CO 2 -enriched treatment gas; and

e) recycling the CO 2 -enriched treatment gas that has been passed through the PTSA and admixing same with the methane-containing gas in step a),

wherein at least a portion of the treatment gas is initially recycled to the first heat exchanger to cool the methane-containing gas in the first heat exchanger before being passed to the PTSA for regeneration.

2. The process as claimed in claim 1 , wherein before step d) the methane-enriched product gas is entirely or at least partially liquefied by cooling to obtain a liquefied methane-enriched product gas.

3. The process as claimed in claim 2 , wherein to achieve at least partial liquefaction the methane-enriched product gas is cooled to −140° C. to −100° C.

4. The process as claimed in claim 2 , wherein the liquefied methane-enriched product gas is decompressed to obtain a flash gas and a decompressed liquefied methane-enriched product gas, wherein the flash gas is passed through the PTSA as treatment gas.

5. The process as claimed in claim 1 , wherein in step b) the CO 2 concentration of the methane-containing gas is reduced to below 6000 ppm.

6. The process as claimed in claim 1 , wherein in step c) the CO 2 concentration of the methane-enriched product gas is reduced to below 5200 ppm.

7. The process as claimed claim 1 , wherein the treatment gas is decompressed and heated before it is passed through the PTSA in step d) as decompressed and optionally heated treatment gas.

8. The process as claimed in claim 7 , wherein after being passed through the PTSA in step d) and before being recycled and admixed with the methane-containing gas in step e), the decompressed and optionally heated treatment gas is compressed to the pressure of the methane-containing gas.

9. The process as claimed in claim 1 , wherein the treatment gas of step d) is used to cool the PTSA after regeneration thereof.

10. The process as claimed in claim 1 , wherein the methane-containing gas is supplied to the PTSA at a pressure of 5-25 bar.

11. The process as claimed in claim 10 , wherein the methane-containing gas is supplied to the PTSA at a temperature of −130° C. to −80° C.

12. The process as claimed in claim 1 , wherein the methane-enriched product gas respectively the liquefied product gas is decompressed before diversion of the treatment gas.

13. The process as claimed in claim 1 , wherein the methane-containing gas in step a) has a CO 2 concentration of not more than 60%.

14. The process as claimed in claim 4 , wherein the decompressed liquefied methane-enriched product gas is passed through a particulate filter, which removes solids from the decompressed liquefied methane-enriched product gas.

15. The process as claimed in claim 1 , wherein the further cooling in step b) is carried out in a second heat exchanger.

Assignments (2)

Priority Claims (1)

Continuity (1)

References Cited (13)