公开(公告)号：EP2590894A1

公开(公告)日：2013-05-15

申请号：EP11734202.2

申请日：2011-06-29

申请人： Eco Technol Pty Ltd

发明人： LIEN, Larry ,  TRANQUILLA, James M. ,  PICARO, Tony

IPC分类号： C01B3/34 ,  C01B3/48 ,  B01D53/22

CPC分类号： C07C1/0485 ,  B01D53/22 ,  B01D53/225 ,  B01D53/228 ,  B01D2256/245 ,  B01D2257/504 ,  C01B3/342 ,  C01B3/48 ,  C01B2203/0222 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/062 ,  C01B2203/0861 ,  C01B2203/1241 ,  C01B2203/1258 ,  Y02C10/10 ,  Y02C20/20 ,  Y02P20/152

摘要： Streams (11) of natural gas contaminated with significant amounts of carbon dioxide can be efficiently and economically processed to create Syngas (16). An available source (1) of flue gas that might otherwise be dispersed into the atmosphere in conjunction with such a CO2-laden natural gas stream (11) renders the process even more economical and efficient through the creation of multiple feedstreams (14, 27, 34) that are combined to deliver a composite near equal mixture of methane and CO2 to a plasma reactor (15) or the like that will generate Syngas. When coupled with a Fischer-Tropsch reactor (40), the overall process provides a particularly efficient and economical process for producing synthetic liquid hydrocarbons.

公开(公告)号：EP2590894B1

公开(公告)日：2016-03-23

申请号：EP11734202.2

申请日：2011-06-29

申请人： Eco Technol Pty Ltd

发明人： LIEN, Larry ,  TRANQUILLA, James M. ,  PICARO, Tony

IPC分类号： C01B3/34 ,  C01B3/48 ,  B01D53/22 ,  C07C1/04

CPC分类号： C07C1/0485 ,  B01D53/22 ,  B01D53/225 ,  B01D53/228 ,  B01D2256/245 ,  B01D2257/504 ,  C01B3/342 ,  C01B3/48 ,  C01B2203/0222 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/062 ,  C01B2203/0861 ,  C01B2203/1241 ,  C01B2203/1258 ,  Y02C10/10 ,  Y02C20/20 ,  Y02P20/152

摘要： Streams (11) of natural gas contaminated with significant amounts of carbon dioxide can be efficiently and economically processed to create Syngas (16). An available source (1) of flue gas that might otherwise be dispersed into the atmosphere in conjunction with such a CO2-laden natural gas stream (11) renders the process even more economical and efficient through the creation of multiple feedstreams (14, 27, 34) that are combined to deliver a composite near equal mixture of methane and CO2 to a plasma reactor (15) or the like that will generate Syngas. When coupled with a Fischer-Tropsch reactor (40), the overall process provides a particularly efficient and economical process for producing synthetic liquid hydrocarbons.