Thermochemical reactor system for a temperature swing cyclic process with integrated heat recovery and a method for operating the same

Patent metadata

Field	Value
Publication number	US-11565229-B2
Application number	US-201716342262-A
Country	US
Kind code	B2
Filing date	Oct 10, 2017
Priority date	Oct 17, 2016
Publication date	Jan 31, 2023
Grant date	Jan 31, 2023

Abstract

Disclosed is a thermochemical reactor system and method for a temperature swing cyclic process with integrated heat recovery having at least two modules, wherein each module includes at least one chemical reaction zone and at least one thermal energy storage unit. The at least two modules are operationally connected for at least one heat transfer fluid for transporting heat between the two modules. Each chemical reaction zone includes at least one reacting material that undergoes in a reversible manner an endothermic reaction at temperature Tendo and an exothermic reaction at temperature Texo, wherein Tendo and Texo differ from each other. The at least one reacting material is provided in at least one encapsulation within each of the chemical reaction zones such that a contact of the reacting material and the at least one heat transfer fluid is avoided.

First claim

The invention claimed is:

1. A thermochemical reactor system for a temperature swing cyclic process with integrated heat recovery comprising:
at least two modules, wherein each module comprises at least one chemical reaction zone (CRZ) and at least one thermal energy storage unit (TES);
wherein the at least two modules are operationally connected for at least one heat transfer fluid (HTF) for transporting heat between the two modules;
wherein each chemical reaction zone (CRZ) comprises at least one reacting material that undergoes in a reversible manner an endothermic reaction at temperature T endo and an exothermic reaction at temperature T exo , wherein T endo and T exo differ from each other;
wherein the at least one reacting material is provided in at least one encapsulation within each of the chemical reaction zones (CRZ) such that a contact of the reacting material and the at least one heat transfer fluid is avoided.

2. The reactor system according to claim 1 , wherein the at least one reacting material in each chemical reaction zone is at least one metal oxide undergoing reduction at reduction temperature T red and oxidation at oxidation temperature T ox , wherein T red and T ox differ from each other.

3. The reactor system according to claim 1 , wherein the at least one reacting material in each chemical reaction zone is at least one material undergoing adsorption at adsorption temperature T adsorp and desorption at desorption temperature T desorb of at least one compound.

4. The reactor system according to claim 1 , wherein the at least one reacting material in each chemical reaction zone is at least one material undergoing carbonation by reacting with CO2 at carbonation temperature T carb and de-carbonation by releasing CO 2 at de-carbonation temperature T decarb of at least one compound, wherein T carb and T decarb differ from each other.

5. The reactor system according to claim 1 , wherein each chemical reaction zone is arranged adjacent to the corresponding thermal energy storage unit (TES).

6. The reactor system according to claim 1 , wherein the at least one encapsulation containing the reacting material is arranged perpendicular, parallel or in any other angle to the flow direction of the HTF through the at least one chemical reaction zone.

7. The reactor system according to claim 1 , wherein the at least one encapsulation is provided in form of at least one tube, a tube bundle or a chamber.

8. The reactor system according to claim 1 , wherein the reacting material is provided in at least two encapsulations.

9. The reactor system according to claim 8 , wherein the encapsulations are arranged parallel and/or perpendicular to each other.

10. The reactor system according to claim 1 , wherein the encapsulation is made of a material with a good thermal conductivity.

11. The reactor system according to claim 1 , wherein at least two reacting materials with different reduction/oxidation temperatures or different adsorption/desorption temperatures or different carbonation/decarbonation temperatures are used, wherein the different reacting materials are arranged in series along the flow direction of the HTF.

12. The reactor system according to claim 11 , wherein each of the different reacting material is arranged in a tube or stack such that a temperature gradient is created between the different reacting materials.

13. The reactor system according to claim 1 , wherein the thermal energy storage units store thermal energy in the form of sensible heat (SHS) and/or latent heat (LHS), and/or heat of reaction of reversible thermochemical reactions (TCS).

14. The reactor system according to claim 1 , wherein the thermal energy storage units comprise a heat storage material comprising a porous structure made of a ceramic material in the form of bricks, channels, pellets, or spheres made of zirconia, silica, or alumina.

15. The reactor system according to claim 1 , wherein the reactor system is coupled to at least one external source of thermal energy (ESE) for heating the HTF.

16. The reactor system according to claim 15 , wherein the external source of thermal energy obtains process heat from a solar receiver and/or electrical heating elements and/or plasma torches and/or combustion of fuels.

17. The reactor system according to claim 1 , wherein the heat transfer fluid (HTF) is air, carbon dioxide, helium, steam, molten salt, molten metals, molten glass, nitrogen, argon, synthetic oils.

18. A method for operating the reactor system according to claim 1 , wherein one of the two chemical reaction zones is operated at the temperature T endo of the endothermic reaction and the other chemical reaction zone is operated at the temperature T exo of the exothermic reaction of the reacting material, wherein the heat required for the chemical reaction zones is provided by a heat transfer fluid.

19. The method according to claim 18 , wherein one of the two chemical reaction zones is operated at the reduction temperature T red and the other chemical reaction zone is operated at the oxidation temperature T0x of a metal oxide used as reacting material.

20. The method according to claim 19 , wherein the metal oxide as reacting material is used for converting water and carbon dioxide to syngas comprising hydrogen and carbon monoxide or for converting methane, water, and carbon dioxide to syngas comprising hydrogen and carbon monoxide.

21. The method according to claim 19 , wherein the metal oxide as reacting material is used for converting water and carbon dioxide to hydrocarbons.

22. The method according to claim 19 , wherein the metal oxide as reacting material is used for the separation of oxygen from air or from any other gas mixtures.

23. The method according to claim 18 , wherein one of the two chemical reaction zones is operated at the adsorption temperature T adsorp and the other chemical reaction zone is operated at the desorption temperature T desorb of the reacting material.

24. The method according to claim 23 , wherein the adsorbing/desorbing reacting material is used for the separation of carbon dioxide and/or water from air or from any other gas mixtures containing any of these compounds.

25. The method according to claim 18 , wherein one of the two chemical reaction zones is operated at the carbonation temperature T carb and the other chemical reaction zone is operated at the decarbonation temperature T decarb of the reacting material.

26. The method according to claim 25 , wherein the carbonation/decarbonation reacting material is used for the separation of carbon dioxide from gas mixtures containing any of these compounds.

27. The method according to claim 18 , wherein the heat transfer fluid is heated by the external source of thermal energy.

28. The method according to claim 18 , wherein the temperature and temperature profile (thermocline) of the chemical reaction zones is additionally controlled and maintained by extracting, heating and injecting the heated heat transfer fluid at different positions along the chemical reaction zones and/or the thermal energy storage units.

29. The method according to claim 18 , wherein the temperature and temperature profile of the chemical reaction zones is additionally controlled and maintained by extracting HTF from any position of the TES unit to transport the stored heat into the resp

Assignees

• Eth Zuerich
• Eth Zuerich

Inventors

• Steinfeld Aldo
• Furler Philipp
• Haselbacher Andreas
• Geissbühler Lukas

Classifications

• B01J2219/2453

  Plates arranged in parallel · CPC title

• B01J2219/2465

  Two reactions in indirect heat exchange with each other · CPC title

• C01B3/063

  Cyclic methods · CPC title

• B01J19/0013 Primary

  Controlling the temperature of the process · CPC title

• C07C1/02

  from oxides of a carbon (preparation of liquid hydrocarbon mixtures of undefined composition C10G2/00; of synthetic natural gas C10L3/06) · CPC title