Thermochemical regeneration with fuel additions

Patent metadata

Field	Value
Publication number	US-10112860-B1
Application number	US-201715643559-A
Country	US
Kind code	B1
Filing date	Jul 7, 2017
Priority date	Jul 15, 2016
Publication date	Oct 30, 2018
Grant date	Oct 30, 2018

Abstract

Operation of a thermochemical regenerator combustion system in which fuel is fed with furnace flue gas into the regenerators to reduce the oxygen content and optionally to establish a reducing atmosphere in both cycles in which the regenerators operate.

First claim

What is claimed is:

1. A method of carrying out combustion in a furnace, comprising
(A) combusting fuel in a furnace to produce gaseous combustion products which contain oxygen; and
(B) alternately
(1) (i) passing a portion of the gaseous combustion products out of the furnace into a first chamber, feeding hydrocarbon fuel into the first chamber, and reacting the hydrocarbon fuel in the first chamber with oxygen present in the gaseous combustion products to reduce the concentration of oxygen in the first chamber and to produce a gaseous reaction mixture containing oxygen and from zero up to 20,000 ppm of carbon monoxide;
(ii) passing the gaseous reaction mixture out of the first chamber into and through a cooled first regenerator to heat the first regenerator and cool said gaseous reaction mixture;
(iii) passing at least part of said cooled gaseous reaction mixture from said first regenerator, and fuel, into a heated second regenerator and, in the second regenerator, reacting the gaseous reaction mixture and the fuel in an endothermic reaction in the second regenerator to form syngas comprising hydrogen and CO; and
(iv) passing said syngas formed in the second regenerator into said furnace and combusting the syngas with one or more oxidant streams injected into said furnace; and
(2) (i) passing a portion of the gaseous combustion products out of the furnace into a second chamber, feeding hydrocarbon fuel into the second chamber, and reacting the hydrocarbon fuel in the second chamber with oxygen present in the gaseous combustion products to reduce the concentration of oxygen in the second chamber and to produce a gaseous reaction mixture containing oxygen and from zero up to 20,000 ppm of carbon monoxide;
(ii) passing the gaseous reaction mixture out of the second chamber into and through a cooled second regenerator to heat the second regenerator and cool said gaseous reaction mixture;
(iii) passing at least part of said cooled gaseous reaction mixture from said second regenerator, and fuel, into a heated first regenerator and, in the first regenerator, reacting the gaseous reaction mixture and the fuel in an endothermic reaction in the first regenerator to form syngas comprising hydrogen and CO; and
(iv) passing said syngas formed in the first regenerator into said furnace and combusting the syngas with one or more oxidant streams injected into said furnace.

2. The method of claim 1 wherein the gaseous combustion products that are passed alternately into the first and second chambers in steps (B)(1)(i) and (B)(2)(i) contain more than 5 vol. % of oxygen, and the gaseous reaction mixture that is formed alternately in the first and second chambers contains up to 5 vol. % of oxygen and contains from zero up to 3000 ppm of carbon monoxide.

3. The method of claim 2 wherein the gaseous reaction mixture that is formed alternately in the first and second chambers contains 0.5 to 2.0 vol. % of oxygen.

4. The method of claim 1 wherein the gaseous reaction mixture that is formed alternately in the first and second chambers in steps (B)(1)(i) and (B)(2)(i) contains less than 20,000 ppm of oxygen and at least 1000 ppm of carbon monoxide.

5. The method of claim 4 wherein the gaseous reaction mixture that is formed alternately in the first and second chambers in steps (B)(1)(i) and (B)(2)(i) contains less than 1,000 ppm of oxygen and 1,000 to 50,000 ppm of carbon monoxide.

6. The method of claim 1 wherein the cooled gaseous reaction mixture that is passed from the first regenerator, or from the second regenerator, or from both regenerators, is reacted with oxygen to reduce the amount of carbon monoxide and hydrocarbons present therein.

7. The method of claim 6 wherein the said reaction with oxygen reduces the amount of carbon monoxide in the cooled gaseous reaction mixture to less than 500 ppm.

8. The method of claim 6 wherein the said reaction with oxygen reduces the amount of carbon monoxide in the cooled gaseous reaction mixture to less than 200 ppm.

9. The method of claim 6 wherein the said reaction with oxygen reduces the amount of carbon monoxide in the cooled gaseous reaction mixture to less than 100 ppm.

10. The method of claim 1 wherein the combustion in the furnace in steps (A) and (B) is carried out with oxidant comprising at least 50 vol. % oxygen.

11. The method of claim 1 wherein the combustion in the furnace in steps (A) and (B) is carried out with oxidant comprising at least 80 vol. % oxygen.

12. The method of claim 1 wherein the furnace is also heated by combustion at one or both of air-fuel burners and/or air-heating regenerators.

13. The method of claim 12 wherein the combined concentration of CO2 and H2O in the flue gas entering the thermochemical regenerators is at least 35 vol. %.

14. The method of claim 12 wherein the combined concentration of CO2 and H2O in the flue gas entering the thermochemical regenerators is greater than 50 vol. %.

Assignees

• Kobayashi Hisashi
• Wu Kuang Tsai
• Praxair Technology Inc

Inventors

• Kobayashi Hisashi
• Wu Kuang-Tsai

Classifications

• C01B3/344 Primary

  using non-catalytic solid particles · CPC title

• C01B2203/0216

  containing a non-catalytic steam reforming step · CPC title

• C01B2203/0811

  by combustion of fuel · CPC title

• C01B2203/044

  Selective oxidation of carbon monoxide · CPC title

• C01B2203/047

  the impurity being carbon monoxide · CPC title