IP Library Granted Patent US 11,325,090
Granted Patent B1
US 11,325,090 · App. 17/097,048 · Granted May 10, 2022

Catalytic solar reactor

Inventors: Jeffrey G Weissman (Guilford, CT); Bruce Crowder (Hamden, CT); Julian Prada (Philadelphia, PA)
Assignee: Precision Combustion, Inc.
B01J12/007B01J19/0013B01J19/127B01J19/2495C01B3/384C01B3/48C07C1/041B01J2219/00076B01J2219/00157C01B2203/0233C01B2203/0238C01B2203/0283C01B2203/062C01B2203/0811C01B2203/0833C01B2203/1241
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Quick Facts
Patent No.
US 11,325,090
App. No.
17/097,048
Granted
May 10, 2022
Kind
B1
Abstract

A catalytic solar reactor useful in chemical processes, more particularly, useful in endothermic chemical processes. The reactor comprises a reaction pathway defined by an exterior wall and an interior wall, the exterior wall comprising a solar radiation receiver capable of converting solar radiation into heat and transmitting the heat to the reaction pathway. Further, the reaction pathway has disposed therein, in alternating fashion, a plurality of catalytic elements and a plurality of heat transfer elements. Optionally, a supplementary heater, such as a conventional fossil fuel burner, is disposed in a plenum located within the interior of the reactor. The heater is employed as a supplemental source of heat, for example, when solar radiation is unavailable.

Claims (26)

1. A catalytic solar reactor comprising a reaction pathway having a reactor inlet and a reactor outlet, the reaction pathway defined by an exterior wall and an interior wall; wherein the exterior wall comprises a solar radiation receiver disposed in thermal communication with the reaction pathway; and further wherein the reaction pathway has disposed therein the following structures:

(a) a plurality of catalytic elements, each catalytic element comprising a porous material having a catalyst supported thereon, each catalytic element further comprising a first flowpath from a first inlet side to a first outlet side;

(b) a plurality of heat transfer elements directly attached to said exterior wall, each heat transfer element comprising at least one porous, thermally-conductive material substantially lacking catalytic activity; each heat transfer element further comprising a second flowpath from a second inlet side to a second outlet side; and

(c) further such that the plurality of catalytic elements and the plurality of heat transfer elements are disposed within the reaction pathway in an alternating configuration defining a fluid flowpath from each element inlet side to each element outlet side.

2. The catalytic solar reactor of claim 1 wherein under operating conditions, the reactor functions via passive thermal conduction from the solar radiation receiver to the reaction pathway.

3. The catalytic solar reactor of claim 1 wherein under operating conditions, the reactor operates essentially isothermally within the plurality of catalytic elements.

4. The catalytic solar reactor of claim 1 wherein each of the plurality of catalytic elements is independently selected from metallic and ceramic materials.

5. The catalytic solar reactor of claim 4 wherein each of the plurality of catalytic elements is provided in the form of a mesh.

6. The catalytic solar reactor of claim 5 wherein the mesh has an ultra-short-channel-length ranging from 25 microns to 500 microns.

7. The catalytic solar reactor of claim 5 wherein the mesh comprises from 100 to 1,000 flow channels per square centimeter.

8. The catalytic solar reactor of claim 4 wherein each of the plurality of catalytic elements comprises a structured material having from 5 to 80 pores per inch.

9. The catalytic solar reactor of claim 1 wherein each of the plurality of catalytic elements independently comprises a set of from 1 to 5 catalytic elements.

10. The catalytic solar reactor of claim 1 wherein the catalyst is selected from a dry reforming catalyst or a Fisher-Tropsch catalyst.

11. The catalytic solar reactor of claim 1 wherein each of the plurality of heat transfer elements is independently selected from monolithic honeycombs and ultra-short-channel-length meshes.

12. The catalytic solar reactor of claim 11 wherein the monolithic honeycomb has a channel length ranging from 50 microns to 25 millimeters; or alternatively, the ultra-short-channel-length mesh has a channel length ranging from 25 microns to 500 microns.

13. The catalytic solar reactor of claim 1 wherein each of the plurality of heat transfer elements is constructed from a metallic composition.

14. The catalytic solar reactor of claim 1 wherein each of the plurality of heat transfer elements independently comprises a set of from 1 to 5 heat transfer elements.

15. The catalytic solar reactor of claim 1 wherein each of the plurality of heat transfer elements comprises no catalyst; or alternatively, comprises a catalyst in an amount less than 0.5 percent, based on total weight of the heat transfer element plus catalyst, so as to facilitate less than 1 percent additional conversion or yield under operating conditions.

16. The catalytic solar reactor of claim 1 wherein a thickness of each catalytic element ranges from 1 percent to 100 percent of a thickness of each heat transfer element.

17. The catalytic solar reactor of claim 1 wherein a total length occupied by the plurality of catalytic elements ranges from 1 percent to 50 percent of a total length of the sum of the catalytic elements plus the heat transfer elements.

18. The catalytic solar reactor of claim 1 wherein a thickness of a set of catalytic elements ranges from 75 microns to 6.3 millimeters, and a thickness of a set of heat transfer elements ranges from 75 microns to 25 millimeters.

19. The catalytic solar reactor of claim 1 wherein the solar radiation receiver is capable of receiving from 100 to 500 kW/m 2 solar irradiance, based on a planar receiver area normal to the direction of direct or reflected solar irradiance.

20. The catalytic solar reactor of claim 1 wherein the solar radiation receiver is capable of adsorbing from 50 percent to 100 percent of irradiated energy.

21. The catalytic solar reactor of claim 1 wherein the solar radiation receiver is constructed with planar dimensions, normal to direct or reflected solar irradiance, of from 1 m 2 to 200 m 2 .

22. The catalytic solar reactor of claim 1 wherein a supplemental heater is disposed within an interior plenum of the catalytic solar reactor.

23. The catalytic solar reactor of claim 22 wherein the supplemental heater is a fossil fuel burner.

Assignments (2)
CONFIRMATORY LICENSE Recorded May 7, 2021
From: PRECISION COMBUSION INC
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 056181/0045 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 13, 2020
From: WEISSMAN, JEFFREY G; CROWDER, BRUCE; PRADA, JULIAN
To: PRECISION COMBUSTION INC
Reel/Frame 054356/0562 →
Continuity (1)
Provisional Application 62945309 · Dec 9, 2019