US2015056112A1PendingUtilityA1

Method and system for synthesizing liquid hydrocarbon compounds

Assignee: JAPAN OIL GAS & METALS JOGMECPriority: Mar 27, 2009Filed: Oct 31, 2014Published: Feb 26, 2015
Est. expiryMar 27, 2029(~2.7 yrs left)· nominal 20-yr term from priority
Inventors:Kazuhiko Tasaka
C10G 45/02C01B 2203/0415C10G 2400/06C01B 2203/043C10G 2/30C01B 2203/148C10K 1/005C10G 2300/1022C01B 2203/047B01D 53/77C01B 2203/146C01B 2203/0233C01B 2203/0894C10G 2400/02C01B 2203/062C10K 1/08B01D 2257/504C10G 65/04C10G 2/342C10G 47/00C10K 1/143C01B 2203/0475C10G 2400/04C01B 2203/0811C10G 2400/08C01B 3/52C10G 2/32C10G 2/344C10G 65/14C07C 1/041Y02P20/151
57
PatentIndex Score
0
Cited by
0
References
0
Claims

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

exact text as granted — not AI-modified
1 - 7 . (canceled) 
     
     
         8 . A system for synthesizing liquid hydrocarbon compounds, comprising:
 a reactor configured to synthesize liquid hydrocarbon compounds from a synthesis gas containing carbon monoxide gas and hydrogen gas by a Fischer-Tropsch synthesis reaction;   a first absorption tower in which a first absorbent absorbs carbon dioxide gas contained in gaseous by-products generated in the reactor;   a second absorption tower in which a second absorbent absorbs a carbon dioxide gas included in the synthesis gas to be supplied to the reactor; and   a second supplying section through which the first absorbent discharged from the first absorption tower is supplied to the second absorption tower.   
     
     
         9 . The system for synthesizing liquid hydrocarbon compounds according to  claim 8 , further comprising
 a merging section configured to merge the gaseous by-products from which the carbon dioxide gas removed by the first absorbent in the first absorption tower into the synthesis gas from which the carbon dioxide gas removed by the second absorbent in the second absorption tower, and which is to be supplied to the reactor.   
     
     
         10 . The system for synthesizing liquid hydrocarbon compounds according to  claim 8 , further comprising
 a regeneration tower in which the carbon dioxide gas is stripped from the second absorbent discharged from the second absorption tower to regenerate the second absorbent.   
     
     
         11 . The system for synthesizing liquid hydrocarbon compounds according to  claim 10 , further comprising
 a first supplying section through which the second absorbent discharged from the regeneration tower is supplied to the first absorption tower to use as the first absorbent in the first absorption tower.   
     
     
         12 . (canceled) 
     
     
         13 . The system for synthesizing liquid hydrocarbon compounds according to  claim 12 , wherein
 the first supplying section includes a first supplying port of the absorbent which is connected to the second absorption tower and through which the absorbent is supplied to the second absorbent tower from the first absorption tower,   the second supplying section includes a second supplying port of the absorbent which is connected to the second absorption tower and through which the absorbent is supplied to the second absorbent tower from the regeneration tower, and   the second supplying port is located downstream in a flow of the synthesis gas in the second absorption tower with respect to the first supplying port on the second absorption tower.   
     
     
         14 . The system for synthesizing liquid hydrocarbon compounds according to  claim 8 ,
 wherein the second absorption tower is configured so that the synthesis gas flows in a direction opposite to the absorbent.

Join the waitlist — get patent alerts

Track US2015056112A1 — get alerts on status changes and closely related new filings.

We store only your email — no account needed. See our privacy policy.