IP Library › Granted Patent US 8,075,870
Granted Patent B2
US 8,075,870 · App. 11/993,889 · Granted Dec 13, 2011

Process for obtaining hydrogen from natural gas

Assignee: Universidad Del Pais Vasco Euskal Herriko Unibertsitatea
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Quick Facts
Patent No.
US 8,075,870
App. No.
11/993,889
Granted
Dec 13, 2011
Kind
B2
Abstract

The invention relates to a process for obtaining hydrogen from natural gas which comprises (a) reacting the natural gas with a mixture of air and steam in a single reactor to obtain a gas comprising H 2 and CO, (b) reacting the CO produced at a high temperature with steam to obtain a gas comprising H 2 and CO 2 , and (c) reacting the CO which has not reacted in step (b) at a low temperature with steam to obtain a gas comprising H 2 and CO 2 , characterized in that in step (a) the natural gas, the air and the steam are fed simultaneously and react on the same catalyst and in that the pressure used in steps (a) to (c) varies between 1 and 8 atm, as well as to a H 2 production plant for carrying out the mentioned process.

Claims (22)

1. A process for obtaining hydrogen from natural gas, the process comprising the steps of:

a. reacting the natural gas with a mixture of air and steam in a single reactor to obtain a gas comprising hydrogen and carbon monoxide,

b. reacting the carbon monoxide produced in step (a) at a high temperature with steam to obtain a gas comprising hydrogen and carbon dioxide, and

c. reacting the carbon monoxide which has not reacted in step (b) at a low temperature with steam to obtain a gas comprising hydrogen and carbon dioxide,

wherein in step (a) the natural gas, the air and the steam are fed simultaneously with an O 2 /CH 4 feed ratio varying between 0.4 and 0.7 and a H 2 O/CH 4 feed ratio varying between 0.8 and 2.5 and react on the same catalyst at a space velocity comprised between 70,000 and 90,000 h −1 , and in that the pressure used in steps (a) to (c) varies between 1 and 8 atm.

2. A process for obtaining hydrogen from natural gas according to claim 1 , comprising an O 2 /CH 4 feed ratio of 0.5 and a H 2 O/CH 4 feed ratio of 2.

3. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the pressure used in steps (a) to (c) is 4 atm.

4. A process for obtaining hydrogen from natural gas according to claim 1 , wherein step (a) is carried out at a temperature varying between 500 and 1000° C.

5. A process for obtaining hydrogen from natural gas according to claim 4 , wherein step (a) is carried out at a temperature of 800° C.

6. A process for obtaining hydrogen from natural gas according to claim 1 , wherein step (b) is carried out at a temperature varying between 350 and 450° C.

7. A process for obtaining hydrogen from natural gas according to claim 6 , wherein step (b) is carried out at a temperature of 400° C.

8. A process for obtaining hydrogen from natural gas according to claim 1 , wherein step (c) is carried out at a temperature varying between 175 and 300° C.

9. A process for obtaining hydrogen from natural gas according to claim 8 , wherein step (c) is carried out at a temperature of 200° C.

10. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the feed natural gas is subjected to a prior sulfur compound elimination step.

11. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the excess heat from step (a) is used to preheat the entire feed to the reactor and in that excess heat from steps (b) and (c) is used to produce the steam used.

12. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the gas obtained in step (c) is subjected to a water elimination step.

13. A process for obtaining hydrogen from natural gas according to claim 12 , wherein the water-free gas is subjected to a subsequent purification stage.

14. A process for obtaining hydrogen from natural gas according to claim 1 , wherein steps (b) and (c) take place in two different reactors.

15. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the reactors used are adiabatic fixed bed type reactors.

16. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the space velocity of steps (a) is 80,000 h −1 .

17. A process for obtaining hydrogen from natural gas according to claim 1 , wherein the space velocity of steps (b) and (c) varies between 7,000 and 9,000 h −1 .

18. A process for obtaining hydrogen from natural gas according to claim 17 , wherein the space velocity of steps (b) and (c) is 8,000 h −1 .

Assignments (2)
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE'S NAME AND ADDRESS PREVIOUSLY RECORDED ON REEL 020448 FRAME 0518. ASSIGNOR(S) HEREBY CONFIRMS THE (SEE DOCUMENT FOR DETAILS).. Recorded Aug 18, 2011
From: CAMBRA IBANEZ, JOSE FRANCISCO; ARIAS ERGUETA, PEDRO LUIS; GUEMEZ BILBAO, MARIA BELEN; BARRIO CAGIGAL, VICTORIA LAURA
To: UNIVERSIDAD DEL PAIS VASCO EUSKAL HERRIKO UNIBERTSITATEA
Reel/Frame 026770/0448 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 31, 2008
From: CAMBRA IBANEZ, JOSE FRANCISCO; ARIAS ERGUETA, PEDRO LUIS; GUEMEZ BILBAO, MARIA BELEN; BARRIO CAGIGAL, VICTORIA LAURA
To: UNIVERSIDAD DEL PAIS VASCO EUSKAL HERRIKO UNIBERSITATEA
Reel/Frame 020448/0518 →
Priority Claims (1)
ES 200501548 · Jun 24, 2005 · national
Continuity (1)
Related Publication 20080315158A1 · Dec 25, 2008