IP Library Granted Patent US 8,609,380
Granted Patent B2
US 8,609,380 · App. 13/345,444 · Granted Dec 17, 2013

Sulfide generation process and system for syngas fermentation

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Quick Facts
Patent No.
US 8,609,380
App. No.
13/345,444
Granted
Dec 17, 2013
Kind
B2
Abstract

A process that generates sulfide in production of liquid products from syngas and a system for syngas fermentation including a sulfide generation process to convert feed gas to liquid product, the process including: partially oxidizing high-temperature gas, input gas, and molten sulfur to generate sulfide gas, the high-temperature gas containing oxygen, the input gas containing carbonaceous fuel and the sulfide gas containing hydrogen sulfide, CO, CO 2 , and H 2 ; mixing the sulfide gas with the feed gas to generate mixed gas having a predetermined hydrogen sulfide concentration; providing at least a portion of the mixed gas to a production fermentor containing microorganisms; and converting the mixed gas to the liquid product by contact with the microorganisms.

Claims (28)

1. A process to convert feed gas to liquid product, the process comprising:

partially oxidizing high-temperature gas, input gas, and molten sulfur to generate sulfide gas, the high-temperature gas containing oxygen, the input gas containing a carbonaceous fuel, and the sulfide gas containing hydrogen sulfide, CO, CO 2 , and H 2 ;

mixing the sulfide gas with the feed gas to generate mixed gas having a predetermined hydrogen sulfide concentration;

providing at least a portion of the mixed gas to a production fermentor containing microorganisms; and

converting the mixed gas to the liquid product by contact with the microorganisms.

2. The process of claim 1 further comprising combusting oxygen and burner gas to generate the high-temperature gas, the burner gas comprising at least one of hydrogen and C 1 to C 4 hydrocarbons.

3. The process of claim 2 wherein the burner gas comprises natural gas.

4. The process of claim 1 further comprising:

providing another portion of the mixed gas to a seed fermentor;

growing a culture of the microorganisms in the seed fermentor; and

providing the culture to the production fermentor.

5. The process of claim 1 wherein the input gas is selected from the group consisting of methane, syngas, and natural gas.

6. The process of claim 1 wherein the partially oxidizing high-temperature gas, input gas, and molten sulfur is performed at a temperature greater than about 1000° C.

7. The process of claim 1 wherein the predetermined hydrogen sulfide concentration is in the range from about 100 to 1000 ppm.

8. The process of claim 1 wherein the feed gas comprises syngas and the liquid product is selected from the group consisting of ethanol, propanol, and butanol.

9. A process to convert syngas feed to a C 1 to C 4 oxygenated liquid product, the process comprising:

combusting oxygen and burner gas to generate high-temperature gas;

partially oxidizing the high-temperature gas, syngas, and molten sulfur to generate sulfide gas, the high temperature gas containing oxygen, and the sulfide gas containing hydrogen sulfide, CO, CO 2 , and H 2 ;

mixing the sulfide gas with the syngas feed to generate mixed gas having a predetermined hydrogen sulfide concentration;

providing at least a portion of the mixed gas to a production fermentor containing microorganisms; and

converting the mixed gas to the C 1 to C 4 oxygenated liquid product by contact with the microorganisms.

10. The process of claim 9 further comprising:

providing another portion of the mixed gas to a seed fermentor;

growing a culture of the microorganisms in the seed fermentor; and

providing the culture to the production fermentor.

11. The process of claim 9 wherein the partially oxidizing the high-temperature gas, syngas, and molten sulfur is performed at a temperature greater than about 1000° C.

12. The process of claim 9 wherein the predetermined hydrogen sulfide concentration is in the range from about 100 to 1000 ppm.

13. The process of claim 9 wherein the C 1 to C 4 oxygenated liquid product is ethanol.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 16, 2016
From: COSKATA INC.
To: COSKATA (ASSIGNMENT FOR THE BENEFIT OF CREDITORS), LLC.
Reel/Frame 038118/0397 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 16, 2016
From: COSKATA (ASSIGNMENT FOR THE BENEFIT OF CREDITORS), LLC.
To: SYNATA BIO, INC.
Reel/Frame 038118/0733 →
RELEASE OF SECURITY INTEREST Recorded Nov 23, 2015
From: VINOD KHOSLA AND NEERU KHOSLA, TRUSTEES OF THE KFT TRUST DATED NOVEMBER 17, 1986; KHOSLA VENTURES III, LP; ADVANCED TECHNOLOGY VENTURES VII, L.P.; ADVANCED TECHNOLOGY VENTURES VII (B), L.P.; ADVANCED TECHNOLOGY VENTURES VII (C), L.P.; ATV ENTREPRENEURS VII, LP
To: COSKATA, INC.
Reel/Frame 037153/0659 →
SECURITY INTEREST Recorded Oct 23, 2015
From: COSKATA, INC.
To: VINOD KHOSLA AND NEERU KHOSLA, TRUSTEES OF THE KFT TRUST DATED NOVEMBER 17, 1986; KHOSLA VENTURES III, LP; ADVANCED TECHNOLOGY VENTURES VII, L.P.; ADVANCED TECHNOLOGY VENTURES VII (B), L.P.; ADVANCED TECHNOLOGY VENTURES VII (C), L.P.; ATV ENTREPRENEURS VII, LP
Reel/Frame 036933/0596 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2013
From: DU, JIANXIN; DATTA, RATHIN
To: COSKATA, INC.
Reel/Frame 030897/0584 →