Solar thermochemical processing system and method

Patent metadata

Field	Value
Publication number	US-9950305-B2
Application number	US-201213559127-A
Country	US
Kind code	B2
Filing date	Jul 26, 2012
Priority date	Jul 26, 2011
Publication date	Apr 24, 2018
Grant date	Apr 24, 2018

Abstract

A solar thermochemical processing system is disclosed. The system includes a first unit operation for receiving concentrated solar energy. Heat from the solar energy is used to drive the first unit operation. The first unit operation also receives a first set of reactants and produces a first set of products. A second unit operation receives the first set of products from the first unit operation and produces a second set of products. A third unit operation receives heat from the second unit operation to produce a portion of the first set of reactants.

First claim

We claim:

1. A method of providing a solar energy augment to the chemical energy content of a reactant stream, the method comprising:
heating a solar reforming reactor from a solar concentrator, the reactor comprising reactor channels and product return flow channels separated by a middle plate, the middle plate providing both a wall of the reactor channels and wall of the product return flow channels;
preheating reactants in a heat exchanger before entering the reactor;
reacting the reactants in the presence of a catalyst in the reaction channels of the reactor to generate a product stream; and
conveying the product stream from the reaction channels to the product return channels while maintaining thermal contact across the middle plate and between the product stream and the reactants in the reaction zone.

2. The method of claim 1 further comprising combusting the product stream in order to provide heat to a power system or for other unit operations requiring heat.

3. The method of claim 2 wherein the power system or the unit operations requiring heat is a combined cycle, fuel cell or power plant, or a factory or chemical process facility requiring heat for steam generation.

4. The method of claim 1 further comprising providing the reactants to a centerpoint of the reactor and conveying the reactants through the reaction channels to a perimeter of the reactor.

5. The method of claim 1 further comprising exchanging the heat from the product stream with the reactants prior to the reactants entering the reaction zone.

6. The method of claim 1 wherein the product stream output is in thermal contact with the reactant stream intake.

7. The method of claim 1 wherein the solar thermochemical augment is at least 20%, wherein the solar thermochemical augment is measured as the increase in Higher Heating Value in the reacting stream divided by the Higher Heating Value of the reactants, times 100%.

8. The method of claim 1 wherein the product stream comprises syngas.

9. The method of claim 1 wherein the product stream is generated at a solar-to-chemical energy conversion efficiency greater than about 60%, wherein the product stream includes syngas, and wherein the solar thermochemical augment is at least 20%, wherein the solar thermochemical augment is measured as the increase in Higher Heating Value in the reacting stream divided by the Higher Heating Value of the reactants, times 100%.

10. A method of providing a solar energy augment to the chemical energy content of a reactant stream, the method comprising:
heating a solar reforming reactor from a solar concentrator, the reactor comprising reactor channels within a collector plate and product return flow channels within a manifold plate, the plates separated by a middle plate and defining a center and an outer perimeter in one cross section;
preheating reactants in a heat exchanger before providing the reactants to the center of the plates; and
reacting the reactants in the presence of a catalyst in the reaction channels of the collector plate to generate a product stream while providing the reactants and product stream from the center to the outer perimeter of the collector plate.

11. The method of claim 10 wherein the reactor channels are defined within the collector plate to extend from the center of the collector plate to the outer perimeter of the collector plate.

12. The method of claim 11 wherein one cross-sectional area of the reactor channels near the center of the collector plate is less than another cross-sectional area of the reactor channels near the outer perimeter of the collector plate.

13. The method of claim 10 further comprising conveying the product stream from the reaction channels to the product return channels.

14. The method of claim 13 wherein the product return flow channels are defined within the manifold plate to extend from the center of the manifold plate to the outer perimeter of the manifold plate.

15. The method of claim 14 wherein one cross-sectional area of the product return channels near the center of the manifold plate is less than another cross-sectional area of the product return channels near the outer perimeter of the manifold plate.

16. The method of claim 14 further comprising transferring product stream from the reaction channels through openings associated with an outer perimeter of the middle plate to the product return channels.

Assignees

• Wegeng Robert S
• Humble Paul H
• Krishnan Shankar
• Leith Steven D
• Palo Daniel R
• Dagle Robert A
• Battelle Memorial Institute

Inventors

• Wegeng Robert S
• Humble Paul H
• Krishnan Shankar
• Leith Steven D
• Palo Daniel R
• Dagle Robert A

Classifications

• F22B1/006

  using solar heat · CPC title

• C10K3/04

  reducing the carbon monoxide content {, e.g. water-gas shift [WGS]} · CPC title

• B01J19/127 Primary

  Sunlight; Visible light · CPC title

• C01B2203/0283

  containing a CO-shift step, i.e. a water gas shift step · CPC title

• B01J2219/089

  Liquid-solid · CPC title