http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2005043417-A1

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00
filingDate 2004-09-27-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b15d07d230a1ec2b9999e25d9c659eda
publicationDate 2005-02-24-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber US-2005043417-A1
titleOfInvention Reducing CO2 levels in CO2-rich natural gases converted into liquid fuels
abstract Provided is a process for converting CO 2 -rich natural gas into liquid fuel. The process includes introducing a CO 2 -rich natural gas feed stream into a synthesis gas formation reactor and then forming a synthesis gas. At least a portion of the synthesis gas is then introduced into a Fischer-Tropsch reactor. A Fischer-Tropsch process is conducted generating a Fischer-Tropsch product. A naphtha is separated from the Fischer-Tropsch product and introduced into a naphtha reformer. Hydrogen by-product is generated by reforming the naphtha to obtain a C 6 -C 10 product having a hydrogen to carbon ratio less than about 2.0. At least a portion of the hydrogen by-product is recirculated and mixed with the CO 2 -rich natural gas feed stream. The hydrogen by-product mixes with the CO 2 -rich natural gas feed stream such that at least a portion of the CO 2 present in the natural gas feed stream is converted into additional CO by a reverse water gas shift reaction so that the synthesis gas derived from the feed stream contains a volume amount of CO 2 that is less than a volume amount of CO 2 present in the feed stream prior to mixing with the hydrogen by-product. Finally, the additional CO is converted into hydrocarbons in the Fischer-Tropsch reactor.
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