IP Library Granted Patent US 8,877,821
Granted Patent B2
US 8,877,821 · App. 13/138,675 · Granted Nov 4, 2014

Method and system for synthesizing liquid hydrocarbon compounds

Inventor: Kazuhiko Tasaka (Tokyo, JP)
Assignees: Japan Oil, Gas and Metals National Corporation; INPEX Corporation; JX Nippon Oil & Energy Corporation; Japan Petroleum Exploration Co., Ltd.; Cosmo Oil Co., Ltd.; Nippon Steel Engineering Co., Ltd.
C10G2/32C01B3/52C10K1/005C10G2400/06C10G2400/08C10G65/14C01B2203/0233C10G2400/02C01B2203/062B01D53/77C10G2/30B01D2257/504C10G65/04C01B2203/0415C10G2/342C10G45/02C01B2203/148C01B2203/043C01B2203/0894C01B2203/047C01B2203/146C10K1/143C10K1/08C01B2203/0811C01B2203/0475C10G2/344C10G2400/04C10G47/00C10G2300/1022
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Quick Facts
Patent No.
US 8,877,821
App. No.
13/138,675
Granted
Nov 4, 2014
Kind
B2
Abstract

Provided is a method for synthesizing liquid hydrocarbon compounds wherein synthesizing liquid hydrocarbon compounds from a synthesis gas by a Fisher-Tropsch synthesis reaction. The method includes a first absorption step of absorbing a carbon dioxide gas, which is contained in gaseous by-products generated in the Fisher-Tropsch synthesis reaction, with an absorbent, and a second absorption step of absorbing a carbon dioxide gas, which is contained in the synthesis gas, with the absorbent which is passed through the first absorption step.

Claims (21)

1. A method for synthesizing liquid hydrocarbon compounds comprising:

a synthesis step of synthesizing liquid hydrocarbon compounds from a synthesis gas containing carbon monoxide gas and hydrogen gas by a Fisher-Tropsch synthesis reaction in a reactor;

a discharge step of discharging gaseous by-products formed by the Fisher-Tropsch synthesis reaction from the reactor;

a first absorption step of absorbing carbon dioxide gas contained in the gaseous by-products discharged from the reactor with a first absorbent; and

a second absorption step of absorbing carbon dioxide gas contained in the synthesis gas to be supplied to the reactor, with a second absorbent; and

a supply step of supplying the first absorbent which has passed through the first absorption step to the second absorption step as the second absorbent.

2. The method for synthesizing liquid hydrocarbon compounds according to claim 1 , further comprising a merging step of merging the gaseous by-products from which the carbon dioxide gas has been removed by the first absorbent into the synthesis gas from which the carbon dioxide gas has been removed by the second absorbent, and which is to be supplied to the reactor.

3. The method for synthesizing liquid hydrocarbon compounds according to claim 1 , further comprising a regenerating step of stripping the carbon dioxide gas from the second absorbent which has passed through the second absorption step to regenerate the second absorbent.

4. The method for synthesizing liquid hydrocarbon compounds according to claim 3 ,

wherein the absorbent which has passed through the regenerating step is used in the first absorption step as the first absorbent.

5. The method for synthesizing liquid hydrocarbon compounds according to claim 3 ,

wherein a part of the absorbent which has passed through the regenerating step is also used in the second absorption step as the second absorbent.

6. The method for synthesizing liquid hydrocarbon compounds according to claim 5 ,

wherein the first absorbent which has passed through the first absorption step is supplied to the synthesis gas in the second absorption step, and thereafter the absorbent which has passed through the regenerating step is supplied to the synthesis gas in the second absorption step.

7. The method for synthesizing liquid hydrocarbon compounds according to claim 1 ,

wherein the synthesis gas flows in a direction opposite to the second absorbent in the second absorption step.

8. The method for synthesizing liquid hydrocarbon compounds according to claim 1 , wherein the absorbent includes aqueous solutions of amine compounds represented by the following formulas (1) to (3),

R 1 R 2 N (CH 2 ) n OH  (1)

R 1 N((CH 2 ) n OH) 2   (2)

N ((CH 2 ) n OH) 3   (3)

wherein R 1 is a hydrogen atom or an alkyl group of C 1 to C 10 , R 2 is a hydrogen atom or an alkyl group of C 1 to C 4 , and n=1 to 5.

Assignments (2)
CHANGE OF NAME Recorded Oct 22, 2014
From: NIPPON STEEL ENGINEERING CO., LTD.
To: NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
Reel/Frame 034030/0769 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 15, 2011
From: TASAKA, KAZUHIKO
To: JAPAN OIL, GAS AND METALS NATIONAL CORPORATION; INPEX CORPORATION; JX NIPPON OIL & ENERGY CORPORATION; JAPAN PETROLEUM EXPLORATION CO., LTD.; COSMO OIL CO., LTD.; NIPPON STEEL ENGINEERING CO., LTD.
Reel/Frame 027062/0749 →
Priority Claims (1)
JP 2009-080490 · Mar 27, 2009 · national
Continuity (1)
Related Publication 20120010304A1 · Jan 12, 2012