Integration of carbon dioxide absorption and water electrolysis into methanation

Patent metadata

Field	Value
Publication number	US-11407693-B2
Application number	US-202117376693-A
Country	US
Kind code	B2
Filing date	Jul 15, 2021
Priority date	Jun 12, 2019
Publication date	Aug 9, 2022
Grant date	Aug 9, 2022

Abstract

A method and system are provided to recover water and carbon dioxide from combustion emissions. The recovery includes, among other things, electrolysis and carbon dioxide capture in a suitable solvent. The recovered water and carbon dioxide are subject to reaction, such as a catalytic methanation reaction, to generate at least methane.

First claim

What is claimed is:

1. A system comprising:
a condenser configured to receive a hydrocarbon combustion exhaust stream comprising water and carbon dioxide and condense steam in the hydrocarbon combustion exhaust stream;
a desiccant dehumidifier configured to receive the hydrocarbon combustion exhaust stream and to remove at least a portion of the water from the hydrocarbon combustion exhaust stream to provide an at least partially dried hydrocarbon combustion exhaust stream;
at least one separation apparatus configured to receive the at least partially dried hydrocarbon exhaust stream and to separate the carbon dioxide from the at least partially dried hydrocarbon combustion exhaust stream, the at least one separation apparatus being configured to capture the carbon dioxide in a solvent, heat the solvent, and separate the carbon dioxide from the heated solvent;
an electrolysis apparatus configured to receive the water removed from the at least partially dried hydrocarbon combustion exhaust stream and to carry out electrolysis on the water to generate hydrogen; and
a reactor configured for conducting a reaction between the generated hydrogen and the separated carbon dioxide to generate one or more hydrocarbons, including at least methane.

2. The system of claim 1 , wherein the condenser is configured to inject the hydrocarbon combustion exhaust stream into liquid water.

3. The system of claim 1 , wherein the condenser comprises a heat exchanger.

4. The system of claim 1 , wherein the at least one separation apparatus comprises:
a first chamber configured to spray the solvent on the at least partially dried hydrocarbon combustion exhaust stream to capture the carbon dioxide in the solvent; and
a second chamber configured to separate the carbon dioxide from the solvent.

5. The system of claim 4 , further comprising a heat pump configured to:
receive the solvent with the carbon dioxide captured therein from the first chamber; and
receive the heated solvent from the second chamber and heat the solvent discharged from the first chamber while cooling the solvent received from the second chamber.

6. The system of claim 1 , further comprising a water purifier configured to boil and distill the water prior to the electrolysis.

7. The system of claim 6 , further comprising conduits to transfer heat generated by the reaction to the water purifier.

8. The system of claim 6 , further comprising conduits to transfer heat from the water purifier to the desiccant dehumidifier.

9. The system of claim 1 , further comprising a compressor for pressurizing the methane and a tank for storing the pressurized methane.

10. The system of claim 1 , wherein the reactor comprises a methanation reactor configured to carry out a catalytic reaction between the generated hydrogen and the separated carbon dioxide to generate the methane.

11. The system of claim 1 , further comprising conduits to transfer oxygen generated by the electrolysis apparatus to a combustion appliance.

12. A system comprising:
a condenser configured to receive a hydrocarbon combustion exhaust stream comprising water and carbon dioxide and condense steam in the hydrocarbon combustion exhaust stream;
a desiccant dehumidifier configured to receive the hydrocarbon combustion exhaust stream and to remove at least a portion of the water from the hydrocarbon combustion exhaust stream to provide an at least partially dried hydrocarbon combustion exhaust stream;
at least one separation apparatus configured to receive the at least partially dried hydrocarbon exhaust stream and to separate the carbon dioxide from the at least partially dried hydrocarbon combustion exhaust stream, the at least one separation apparatus comprising a first chamber configured to capture the carbon dioxide in a solvent;
a heat pump configured to heat the solvent and the captured carbon dioxide;
the at least separation apparatus further comprising a second chamber configured to separate the carbon dioxide from the heated solvent;
an electrolysis apparatus configured to receive the water removed from the at least partially dried hydrocarbon combustion exhaust stream and to carry out electrolysis on the water to generate hydrogen; and
a reactor configured for conducting a reaction between the generated hydrogen and the separated carbon dioxide to generate one or more hydrocarbons, including at least methane.

13. The system of claim 12 , wherein the condenser is configured to inject the hydrocarbon combustion exhaust stream into liquid water.

14. The system of claim 12 , further comprising a water purifier configured to boil and distill the water prior to the electrolysis.

15. The system of claim 14 , further comprising conduits to transfer heat generated by the reaction to the water purifier.

16. The system of claim 14 , further comprising conduits to transfer heat from the water purifier to the desiccant dehumidifier.

17. A system comprising:
a condenser configured to receive a hydrocarbon combustion exhaust stream comprising water and carbon dioxide and condense steam in the hydrocarbon combustion exhaust stream;
a desiccant dehumidifier configured to receive the hydrocarbon combustion exhaust stream and to remove at least a portion of the water from the hydrocarbon combustion exhaust stream to provide an at least partially dried hydrocarbon combustion exhaust stream;
at least one separation apparatus configured to receive the at least partially dried hydrocarbon exhaust stream and to separate the carbon dioxide from the at least partially dried hydrocarbon combustion exhaust stream, the at least one separation apparatus comprising a first chamber configured to capture the carbon dioxide in a solvent;
a heat pump configured to receive the solvent with the captured carbon dioxide from the first chamber;
the at least separation apparatus further comprising a second chamber configured to separate the carbon dioxide from the heated solvent;
the heat pump further configured to receive the heated solvent from the second chamber and to heat the solvent received from the first chamber with the heated solvent received from the second chamber while cooling the heated solvent received from the second chamber;
an electrolysis apparatus configured to receive the water removed from the at least partially dried hydrocarbon combustion exhaust stream and to carry out electrolysis on the water to generate hydrogen; and
a reactor configured for conducting a reaction between the generated hydrogen and the separated carbon dioxide to generate one or more hydrocarbons, including at least methane.

18. The system of claim 17 , further comprising a water purifier configured to boil and distill the water prior to the electrolysis.

19. The system of claim 18 , further comprising conduits to transfer heat generated by the reaction to the water purifier.

20. The system of claim 18 , further comprising conduits to transfer heat from the water purifier to the desiccant dehumidifier.

Assignees

• Standard Carbon Ltd
• Ariel Scient Innovations Ltd
• 1 Standard Carbon Ltd
• 2 Ariel Scient Innovations Ltd

Inventors

• Winkler Nathan H
• Sassoon Michael V
• Golan Gady
• Zerbib Shlomo A

Classifications

• C25B1/04 Primary

  by electrolysis of water · CPC title

• Y02P20/151

  Reduction of greenhouse gas [GHG] emissions, e.g. CO2 · CPC title

• B01J2219/00835

  Comprising catalytically active material · CPC title

• B01D53/28

  Selection of materials for use as drying agents · CPC title

• C02F1/04

  by distillation or evaporation · CPC title