Method of generating clean syngas

Patent metadata

Field	Value
Publication number	US-12077435-B2
Application number	US-202318233028-A
Country	US
Kind code	B2
Filing date	Aug 11, 2023
Priority date	Sep 27, 2011
Publication date	Sep 3, 2024
Grant date	Sep 3, 2024

Abstract

A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

First claim

What is claimed is:

1. A method of generating a clean syngas, the method comprising:
processing carbonaceous material by steam reforming with a recycled carbon dioxide stream as vapor purges to yield a first syngas stream;
performing hydrocarbon reforming on the first syngas stream to yield a second syngas stream;
cooling the second syngas stream to generate steam and to yield a cooled syngas stream;
compressing the cooled syngas stream to yield a compressed syngas stream;
removing one or more metals, ammonia, and/or hydrogen cyanide from the compressed syngas stream;
performing sulfur polishing on the compressed syngas stream;
removing carbon dioxide from the compressed syngas stream to yield a clean syngas stream; and
recycling at least a portion of the removed carbon dioxide to the steam reforming step.

2. The method of claim 1 , wherein said hydrocarbon reforming comprises one or more of an oxidant, a catalyst, and/or a partial oxidative environment.

3. The method of claim 1 , wherein the second syngas stream comprises a syngas having increased amounts of hydrogen (H 2 ) and/or carbon monoxide (CO), as compared to the first syngas stream.

4. The method of claim 1 , wherein the first syngas stream comprises one or more hydrocarbons, and wherein a hydrocarbon reformer converts the one or more hydrocarbons into at least hydrogen (H 2 ) and carbon monoxide (CO).

5. The method of claim 1 , wherein said cooling comprises use of a heat recovery steam generator to remove heat from second syngas stream.

6. The method of claim 1 , further comprising, after said cooling:
scrubbing the cooled syngas stream to remove one or more of solids or contaminants.

7. The method of claim 6 , wherein said scrubbing comprises a venturi scrubber.

8. The method of claim 1 , wherein said compressing comprises a compressor, wherein a syngas is routed to an inlet of the compressor.

9. The method of claim 1 , further comprising:
reacting the clean syngas stream in a Fischer-Tropsch synthesis reactor to yield one or more Fischer-Tropsch products.

10. The method of claim 9 , wherein the one or more Fischer-Tropsch products comprise a medium fraction Fischer-Tropsch liquid.

11. The method of claim 1 , further comprising:
reacting the clean syngas stream to yield one or more synthesis products.

12. The method of claim 11 , wherein the one or more synthesis products comprise methanol, ethanol, or mixed alcohols.

13. The method of claim 11 , wherein the one or more synthesis products comprise a chemical or a chemical intermediate.

Assignees

• Thermochem Recovery Int Inc

Inventors

• Chandran Ravi
• Leo Daniel Michael
• Freitas Shawn Robert
• Newport Dave G
• Whitney Hamilton Sean Michael
• Burciaga Daniel A

Classifications

• C01B2203/147

  Three or more purification steps in series · CPC title

• C01B2203/142

  At least two reforming, decomposition or partial oxidation steps in series · CPC title

• C01B2203/1241

  Natural gas or methane · CPC title

• C01B2203/1235

  Hydrocarbons · CPC title

• C01B2203/0435

  Catalytic purification · CPC title