IP Library › Granted Patent US 11,383,974
Granted Patent B2
US 11,383,974 · App. 17/254,772 · Granted Jul 12, 2022

Method and apparatus for dehydrogenating a hydrogen carrier medium

Inventors: Andreas Bösmann (Hessdorf, DE); Patrick Preuster (Heideck, DE); Peter Wasserscheid (Erlangen, DE); Denise Geburtig (Nuremberg, DE)
Assignee: HYDROGENIOUS LOHC TECHNOLOGIES GMBH
C01B3/0015B01J21/18B01J23/44
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Quick Facts
Patent No.
US 11,383,974
App. No.
17/254,772
Granted
Jul 12, 2022
Kind
B2
Abstract

A method for dehydrogenating a hydrogen carrier medium comprises the method steps of providing a metal-containing catalyst material, an at least partially loaded hydrogen carrier medium, a metal-free reaction accelerator substance, transferring hydrogen from the hydrogen carrier medium to the reaction accelerator substance and releasing hydrogen gas from the reaction accelerator substance.

Claims (27)

1. A method for dehydrogenating a hydrogen carrier medium, the method comprising the method steps of:

providing:

a metal-containing catalyst material;

an at least partially loaded hydrogen carrier medium, and

a metal-free reaction accelerator substance;

transferring hydrogen from the hydrogen carrier medium to the reaction accelerator substance; and

releasing hydrogen gas from the reaction accelerator substance.

2. The method as claimed in claim 1 , further comprising providing a reaction pressure of from 0.001 bar to 50 bar.

3. The method as claimed in claim 1 , further comprising providing a reaction temperature of from 25° C. to 400° C.

4. The method as claimed in claim 1 , wherein the releasing of hydrogen gas is with a release rate of at least 10 standard liters of hydrogen per liter of catalyst volume and per minute at a reaction temperature of less than 250° C.

5. The method as claimed in claim 1 , wherein reaction accelerator substance has at least one functional group which contains at least one of oxygen and nitrogen.

6. The method as claimed in claim 1 , wherein the reaction accelerator substance in the hydrogen-enriched form comprises secondary alcohols of the form

7. The method as claimed in claim 1 , wherein the reaction accelerator substance in the hydrogen-enriched form comprises at least one of oligovinyl alcohols of the form

and polyvinyl alcohols of the form

8. The method as claimed in claim 1 , wherein the reaction accelerator substance in the hydrogen-enriched form comprises secondary amines of the form

9. The method as claimed in claim 1 , wherein the reaction accelerator substance in the hydrogen-enriched form comprises at least one of oligovinylamines and polyvinylamines of the form

10. The method as claimed in claim 1 , wherein reaction accelerator substance in the hydrogen-enriched form comprises a dehydrogenatable heteroalicyclic compound of the form of one of

11. The method as claimed in claim 1 , wherein reaction accelerator substance has a vapor pressure (p R ) which is greater than the vapor pressure (p W ) of the hydrogen carrier medium, wherein p R >1.5 p W .

12. The method as claimed in claim 1 , wherein the reaction accelerator substance has a vapor pressure (p R ) which is lower than the vapor pressure (p W ) of the hydrogen carrier medium, wherein p R <0.8 p W .

13. The method as claimed in claim 1 , wherein the reaction accelerator substance has a miscibility gap with the hydrogen carrier medium at a temperature of at most 50° C.

14. The method as claimed in claim 1 , wherein the reaction accelerator substance is present as a solid.

15. An apparatus for dehydrogenating a hydrogen carrier medium, by providing: a metal-containing catalyst material; an at least partially loaded hydrogen carrier medium, and a metal-free reaction accelerator substance; transferring hydrogen from the hydrogen carrier medium to the reaction accelerator substance; and releasing hydrogen gas from the reaction accelerator substance, the apparatus comprising:

at least one reaction vessel; and

a contacting unit arranged in the at least one reaction vessel.

16. The method as claimed in claim 1 , further comprising providing a reaction pressure of less than 0.1 bar.

17. The method as claimed claim 1 , further comprising providing a reaction temperature of less than 100° C.

18. The method as claimed in claim 1 , wherein the catalyst material has been deposited directly onto the reaction accelerator substance.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 20, 2021
From: BÖSMANN, ANDREAS, DR.; PREUSTER, PATRICK, DR.; WASSERSCHEID, PETER, DR.; GEBURTIG, DENISE
To: HYDROGENIOUS LOHC TECHNOLOGIES GMBH
Reel/Frame 056913/0808 →
Priority Claims (2)
DE 10 2018 210 247.3 · Jun 22, 2018 · national
DE 10 2018 210 337.2 · Jun 25, 2018 · national
Continuity (1)
Related Publication 20210276862A1 · Sep 9, 2021
Cited By (1)
US 12,496,564