IP Library Granted Patent US 7,537,750
Granted Patent B2
US 7,537,750 · App. 10/891,314 · Granted May 26, 2009

Method for producing hydrogen gas by steam methane reforming using solar energy

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Quick Facts
Patent No.
US 7,537,750
App. No.
10/891,314
Granted
May 26, 2009
Kind
B2
Abstract

Hydrogen gas is produced by reacting a carbon-hydrogen-containing species with water provided as a water reforming inflow at a reforming temperature to produce a primary reacted gas flow containing hydrogen gas. The carbon-hydrogen-containing species and water are heated to the reforming temperature with solar energy. The heating is preferably performed by heating a molten metal to at least the reforming temperature with solar energy, and using the molten metal to heat the carbon-hydrogen-containing species and water to at least the reforming temperature. The water reforming inflow is preheated by heat exchange from the primary reacted gas flow. The primary reacted gas flow is reacted with water to produce additional hydrogen gas in a secondary reacted gas flow.

Claims (44)

1. A method for producing hydrogen gas, comprising the steps of:

reacting a carbon-hydrogen-containing species with water provided as a water reforming inflow at a reforming temperature to produce a primary reacted gas flow containing hydrogen gas;

heating the carbon-hydrogen-containing species and water to the reforming temperature with solar energy, wherein the heating includes heating a molten metal to at least the reforming temperature with solar energy, and using the heated molten metal to heat the carbon-hydrogen-containing species and water to at least the reforming temperature;

preheating the water reforming inflow by heat exchange from the primary reacted gas flow; and

reacting the primary reacted gas flow with water to produce additional hydrogen gas in a secondary reacted gas flow.

2. The method of claim 1 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

reacting the carbon-hydrogen-containing species with water in the presence of a catalyst.

3. The method of claim 1 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

providing the carbon-hydrogen-containing species comprising methane.

4. The method of claim 1 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

providing the carbon-hydrogen-containing species comprising an alcohol selected from the group consisting of ethanol and methanol.

5. The method of claim 1 , including an additional step of producing the carbon-hydrogen-containing species by a biomass reaction.

6. The method of claim 1 , wherein the steps of heating and preheating do not involve any burning of a hydrocarbon fuel.

7. The method claim 1 , wherein the step of heating the carbon-hydrogen-containing species includes directing solar rays with at least one heliostat toward a solar heat exchanger.

8. The method of claim 1 , including circulating the molten metal between an insulated holding tank and a reforming reactor for reacting the carbon-hydrogen-containing species, to heat the carbon-hydrogen-containing species.

9. The method of claim 1 , including circulating the molten metal between a first holding tank at a first temperature, a second holding tank at a second temperature that is greater than the first temperature, and a reforming reactor for reacting the carbon-hydrogen-containing species, to heat the carbon-hydrogen-containing species.

10. The method of claim 1 , including establishing a counter-current flow between the heated molten metal and the carbon-hydrogen-containing species through a reforming reactor for reacting the carbon-hydrogen-containing species, to heat the carbon-hydrogen-containing species.

11. A method for producing hydrogen gas, comprising the steps of:

reacting a carbon-hydrogen-containing species with water provided as a water reforming inflow at a reforming temperature of at least 1500.degree. F. and in the presence of a catalyst to produce a primary reacted gas flow containing hydrogen gas;

heating the carbon-hydrogen-containing species and water to the reforming temperature with solar energy, wherein the step of heating includes the steps of

heating a molten metal to at least the reforming temperature with solar energy, and

using the molten metal to heat the carbon-hydrogen-containing species and water to at least the reforming temperature;

preheating the water reforming inflow by heat exchange from the primary reacted gas flow; and

reacting the primary reacted gas flow with water to produce additional hydrogen gas in a secondary reacted gas flow.

12. The method of claim 11 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

providing the carbon-hydrogen-containing species comprising methane.

13. The method of claim 11 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

providing the carbon-hydrogen-containing species comprising an alcohol selected from the group consisting of ethanol and methanol.

14. The method of claim 11 , including an additional step of

producing the carbon-hydrogen-containing species by a biomass reaction.

15. The method of claim 11 , wherein the steps of heating and preheating do not involve any burning of a hydrocarbon fuel.

16. A method for producing hydrogen gas, comprising the steps of:

reacting a carbon-hydrogen-containing species with water provided as a water reforming inflow at a reforming temperature of at least about 1500.degree. F. in the presence of a catalyst in a reforming apparatus to produce a primary reacted gas flow containing hydrogen gas;

heating the carbon-hydrogen-containing species and water to the reforming temperature with solar energy, wherein the step of heating includes the steps of

heating a molten metal to at least the reforming temperature with solar energy, and

using the molten metal to heat the carbon-hydrogen-containing species and water to at least the reforming temperature;

preheating the water reforming inflow by heat exchange from the primary reacted gas flow in a preheat heat exchange; and

reacting the primary reacted gas flow with water in a shift reactor to produce additional hydrogen gas in a secondary reacted gas flow.

17. The method of claim 16 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

providing the carbon-hydrogen-containing species comprising methane.

18. The method of claim 16 , wherein the step of reacting the carbon-hydrogen-containing species with water includes the step of

providing the carbon-hydrogen-containing species comprising an alcohol selected from the group consisting of ethanol and methanol.

19. The method of claim 16 , including an additional step of

producing the carbon-hydrogen-containing species by a biomass reaction.

Assignments (12)
RELEASE OF SECURITY INTEREST Recorded Aug 5, 2016
From: U.S. BANK NATIONAL ASSOCIATION
To: AEROJET ROCKETDYNE OF DE, INC. (F/K/A PRATT & WHITNEY ROCKETDYNE, INC.)
Reel/Frame 039597/0890 →
RELEASE OF SECURITY INTEREST Recorded Sep 23, 2015
From: U.S. BANK NATIONAL ASSOCIATION
To: AEROJET ROCKETDYNE OF DE, INC.
Reel/Frame 036666/0103 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 17, 2014
From: AEROJET ROCKETDYNE OF DE
To: SOLARRESERVE TECHNOLOGY, LLC
Reel/Frame 034530/0978 →
CHANGE OF NAME Recorded May 8, 2014
From: PRATT & WHITNEY ROCKETDYNE, INC.
To: AEROJET ROCKETDYNE OF DE, INC.
Reel/Frame 032845/0909 →
SECURITY AGREEMENT Recorded Jun 21, 2013
From: PRATT & WHITNEY ROCKETDYNE, INC.
To: U.S. BANK NATIONAL ASSOCIATION
Reel/Frame 030656/0615 →
SECURITY AGREEMENT Recorded Jun 17, 2013
From: PRATT & WHITNEY ROCKETDYNE, INC.
To: WELLS FARGO BANK, NATIONAL ASSOCIATION
Reel/Frame 030628/0408 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE'S NAME ON ORIGINAL COVER SHEET PREVIOUSLY RECORDED ON REEL 017882 FRAME 0126. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNEE WAS INCORRECTLY RECORDED AS "UNITED TECHNOLOGIES CORPORATION". ASSIGNEE SHOULD BE "RUBY ACQUISITION ENTERPRISES CO.". Recorded Jun 12, 2013
From: THE BOEING COMPANY AND BOEING MANAGEMENT COMPANY
To: RUBY ACQUISITION ENTERPRISES CO.
Reel/Frame 030592/0954 →
CHANGE OF NAME Recorded Jun 12, 2013
From: RUBY ACQUISITION ENTERPRISES CO.
To: PRATT & WHITNEY ROCKETDYNE, INC.
Reel/Frame 030593/0055 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 8, 2012
From: HAMILTON SUNDSTRAND CORPORATION
To: PRATT & WHITNEY, ROCKETDYNE, INC.
Reel/Frame 029293/0682 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 16, 2006
From: BOEING C OMPANY AND BOEING MANAGEMENT COMPANY, THE
To: UNITED TECHNOLOGIES CORPORATION
Reel/Frame 017882/0126 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 27, 2006
From: BOEING COMPANY AND BOEING MANAGEMENT COMPANY, THE
To: UNITED TECHNOLOGIES CORPORATION
Reel/Frame 017681/0537 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 14, 2004
From: LITWIN, ROBERT ZACHARY; STEWART, ALBERT E.
To: THE BOEING COMPANY
Reel/Frame 015577/0603 →