Cogeneration of chemical products

Patent metadata

Field	Value
Publication number	US-12098658-B2
Application number	US-202318513179-A
Country	US
Kind code	B2
Filing date	Nov 17, 2023
Priority date	Jun 13, 2019
Publication date	Sep 24, 2024
Grant date	Sep 24, 2024

Abstract

The present disclosure relates to cogeneration of power and one or more chemical entities through operation of a power production cycle and treatment of a stream comprising carbon monoxide and hydrogen. A cogeneration process can include carrying out a power production cycle, providing a heated stream comprising carbon monoxide and hydrogen, cooling the heated stream comprising carbon monoxide and hydrogen against at least one stream in the power production cycle so as to provide heating to the power production cycle, and carrying out at least one purification step so as to provide a purified stream comprising predominately hydrogen. A system for cogeneration of power and one or more chemical products can include a power production unit, a syngas production unit, one or more heat exchange elements configured for exchanging heat from a syngas stream from the syngas production unit to a stream from the power production unit, and at least one purifier element configured to separate the syngas stream into a first stream comprising predominately hydrogen and a second stream.

First claim

The invention claimed is:

1. A method for generation of one or more chemical products, the method comprising:
providing a heated stream comprising at least carbon monoxide and hydrogen;
cooling the heated stream comprising at least carbon monoxide and hydrogen such that heat therefrom is transferred to at least one stream and a cooled stream comprising at least carbon monoxide and hydrogen is provided;
subjecting the cooled stream comprising at least carbon monoxide and hydrogen to one or more purification steps so as to provide a first stream comprising predominantly hydrogen and a second stream that is a hydrogen-depleted stream; and
carrying out one or both of the following:
processing the hydrogen-depleted stream so as to recover carbon dioxide therefrom;
combining at least a portion of the first stream comprising predominately hydrogen with nitrogen from a nitrogen source under conditions effective to form ammonia;

wherein the heated stream comprising at least carbon monoxide and hydrogen is a syngas stream that is formed in a syngas generation unit, and wherein heat is provided to the syngas generation unit from a separate unit that comprises a combustor.

2. The method of claim 1 , wherein the syngas generation unit comprises one or more of a gasification unit, a partial oxidation unit, and a reforming unit.

3. The method of claim 1 , wherein the heat that is provided is transferred via a stream comprising carbon dioxide.

4. The method of claim 1 , wherein processing the hydrogen-depleted stream so as to recover carbon dioxide is carried out in a low temperature CO 2 separation unit configured to cool the at least a portion of the hydrogen-depleted stream to a temperature sufficient for separation of the carbon dioxide in a liquefied form.

5. The method of claim 4 , wherein the low temperature CO 2 separation unit is configured to cool the at least a portion of the hydrogen-depleted stream to a temperature that is 2° C. to 25° C. greater than a freezing temperature of the at least a portion of the hydrogen-depleted stream.

6. The method of claim 1 , wherein processing the hydrogen-depleted stream so as to recover carbon dioxide is carried out with a membrane unit.

7. The method of claim 1 , wherein the step of combining at least a portion of the stream comprising predominately hydrogen with nitrogen from a nitrogen source under conditions effective to form ammonia is carried out in an ammonia synthesis unit.

8. The method of claim 7 , wherein the nitrogen source is an air separation unit.

9. The method of claim 8 , wherein oxygen from the air separation is utilized as an oxidant in a syngas generation unit.

10. The method of claim 7 , further comprising combining carbon dioxide with at least a portion of the ammonia in a urea synthesis unit under conditions effective to form urea.

11. The method of claim 1 , wherein the at least one stream to which heat is transferred from the heated stream comprising at least carbon monoxide and hydrogen is a water stream, and the transfer of heat is sufficient to form steam.

12. A system for generation of one or more chemical products, the system comprising:
a first unit comprising a combustor;
a second unit that is a syngas generation unit effective for providing a heated syngas stream, the syngas generation unit being configured to be heated with a combustion exhaust stream from the combustor;
one or more heat exchange elements configured for exchanging heat from the heated syngas stream to at least one stream and providing a cooled syngas stream;
at least one separation unit configured to separate the cooled syngas stream into a first stream comprising predominately hydrogen and a second stream that is a hydrogen-depleted stream; and
one or both of:
one or more lines configured for passing at least a portion of the hydrogen-depleted stream through a separation unit configured to separate carbon dioxide therefrom;
an ammonia synthesis unit configured to receive at least a portion of the first stream comprising predominately hydrogen and to receive a stream comprising nitrogen and form a stream comprising ammonia.

13. The system of claim 12 , further comprising an air separation unit configured for providing the stream comprising nitrogen to the ammonia synthesis unit.

14. The system of claim 12 , further comprising a urea synthesis unit configured to receive at least a portion of the stream comprising ammonia and to receive a stream comprising carbon dioxide and form a stream comprising urea.

15. The system of claim 12 , wherein the separation unit configured to separate carbon dioxide includes one or both of a membrane separator and a pressure swing adsorption unit.

Assignees

• 8 Rivers Capital Llc

Inventors

• Lu Xijia
• Forrest Brock Alan
• Rafati Navid

Classifications

• F01K7/06

  the engines being of multiple-inlet-pressure type (F01K7/02 takes precedence; the engines being only of turbine type F01K7/16; the engines using steam of critical or over-critical pressure F01K7/32; the engines being of extraction or non-condensing type F01K7/34) · CPC title

• F01K25/103 Primary

  Carbon dioxide (F01K25/065 takes precedence) · CPC title

• F01K23/068

  in combination with an oxygen producing plant, e.g. an air separation plant · CPC title

• F01K7/16

  the engines being only of turbine type (the engines using steam of critical or overcritical pressure F01K7/32; the engines being of extraction or non-condensing type F01K7/34) · CPC title

• C01B2203/84

  Energy production · CPC title