IP Library Granted Patent US 9,597,629
Granted Patent B2
US 9,597,629 · App. 14/806,862 · Granted Mar 21, 2017

Method and device for separating off carbon dioxide from a gas mixture

Inventors: Carsten Matthias (Friedrichshafen, DE); Walter Jehle (Horgenzell, DE); Peter Kern (Salem, DE)
Assignee: Airbus DS GmbH
B01D53/053A62B11/00B01D53/0423B01D53/0431B01D53/0462B01D2252/204B01D2253/102B01D2253/20B01D2257/504B01D2258/06B01D2259/4009B01D2259/40013B01D2259/40043B01D2259/40096B01D2259/4566B01D2259/4575Y02C10/04Y02C10/06Y02C10/08
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Quick Facts
Patent No.
US 9,597,629
App. No.
14/806,862
Granted
Mar 21, 2017
Kind
B2
Abstract

A method for separating off carbon dioxide from a gas mixture, in particular from breathing air, with a life-sustaining device, wherein in a first method step the gas mixture is fed to an adsorption and/or absorption unit under at least one first pressure, and in a second method step a gas mixture is conveyed out of the adsorption and/or absorption unit under at least one second pressure that is higher than the first pressure.

Claims (21)

1. A method for separating off carbon dioxide from a gas mixture, in particular from breathing air, with a life-sustaining device, wherein in a first method step the gas mixture is fed to an adsorption and/or absorption unit under at least one first pressure, and in a second method step a gas mixture is conveyed out of the adsorption and/or absorption unit under at least one second pressure that is higher than the first pressure.

2. The method according to claim 1 , wherein in the first method step the gas mixture is fed to the adsorption and/or absorption unit at least substantially at an ambient pressure.

3. The method according to claim 1 , wherein at least one pressure container is used as an adsorption and/or absorption unit.

4. The method according to claim 1 , wherein the adsorption and/or absorption unit is heated for the purpose of a pressure increase inside the adsorption and/or absorption unit.

5. The method according to claim 4 , wherein the adsorption and/or absorption unit is heated by means of hot vapor.

6. The method according to claim 1 , wherein at least one adsorption and/or absorption unit is heated electrically.

7. The method according to claim 1 , wherein a fluid is introduced into the adsorption and/or absorption unit for the purpose of a pressure increase inside the adsorption and/or absorption unit.

8. The method according to claim 5 , wherein hot vapor is introduced for the purpose of a pressure increase inside the adsorption and/or absorption unit.

9. The method according to claim 1 , wherein in the first method step the gas mixture is fed to the adsorption and/or absorption unit under at least one first temperature and in the second method step the gas mixture that is to be conveyed off is conveyed out of the adsorption and/or absorption unit under at least one second temperature that is higher than the first temperature.

10. The method according to claim 1 , wherein a gas is refed to the adsorption and/or absorption unit for the purpose of increasing a concentration in the adsorption and/or absorption unit.

11. The method according to claim 1 , wherein carbon dioxide is conveyed out of at least one adsorption and/or absorption unit without a subsequent densification and without using a compressor.

12. The method according to claim 1 , wherein in at least one adsorption and/or absorption unit at least one volume compensator is used, which is provided for ensuring a compaction of an adsorption and/or absorption material of the adsorption and/or absorption unit.

13. The method according to claim 1 , wherein the gas mixture is introduced into the adsorption and/or absorption unit in a first direction and is conveyed through an adsorption and/or absorption material arranged in the adsorption and/or absorption unit in a second direction that substantially differs from the first direction.

14. The method according to claim 1 , wherein heat energy is transferred from an adsorption and/or absorption unit to at least one further adsorption and/or absorption unit.

15. The method according to claim 1 , wherein pressure energy is transferred from an adsorption and/or absorption unit to at least one further adsorption and/or absorption unit.

16. The method according to claim 1 , wherein at least one solid-matter adsorber and/or solid-matter absorber is used.

17. The method according to claim 1 , wherein at least an amine is used.

18. The method according to claim 1 , wherein a recovery of air from at least one adsorption and/or absorption unit is carried out by means of at least one vacuum pump.

19. The method according to claim 1 , wherein pre-densified carbon dioxide after being conveyed out of at least one adsorption and/or absorption unit is dehydrated and then subsequently densified.

20. The method according to claim 1 , wherein carbon dioxide is dissolved in a liquid by means of at least one pressure water purger.

21. The method according to claim 1 , wherein a residual gas pressure in at least one adsorption and/or absorption unit is discharged into a liquid tank in at least one method step.

Assignments (2)
MERGER Recorded Jan 10, 2019
From: AIRBUS DS GMBH
To: AIRBUS DEFENCE AND SPACE GMBH
Reel/Frame 048043/0373 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 23, 2015
From: MATTHIAS, CARSTEN; JEHLE, WALTER; KERN, PETER
To: AIRBUS DS GMBH
Reel/Frame 036162/0579 →
Priority Claims (1)
EP 14178611 · Jul 25, 2014 · regional
Continuity (1)
Related Publication 20160023157A1 · Jan 28, 2016