发明名称 METHOD FOR IMPROVING FISCHER-TROPSCH SYNTHESIS AND RECYCLING EXHAUST GASES THEREFROM
摘要 A method for improving Fischer-Tropsch synthesis and recycling exhaust gases therefrom. The method includes: 1) transforming raw gas for Fischer-Tropsch synthesis using a water-gas shift reaction, transporting the transformed raw gas to a Fischer-Tropsch synthesis device for Fischer-Tropsch synthesis in the presence of a Fe-based or Co-based catalyst; 2) introducing exhaust gases from the Fischer-Tropsch synthesis device to a first pressure-swing adsorber for hydrogen recovery; 3) introducing the exhaust gases from 2) to a second pressure-swing adsorber for methane recovery; 4) returning part of the hydrogen obtained from 2) to 1) to mix with the raw gas, and transforming a resulting mixed gas to adjust a hydrogen/carbon ratio of the raw gas; and 5) introducing the methane in 3) to a methane reforming device to reform the methane whereby yielding syngas having relatively high hydrogen/carbon ratio, and transporting the syngas to 1) to mix with the raw gas.
申请公布号 US2015099813(A1) 申请公布日期 2015.04.09
申请号 US201414571240 申请日期 2014.12.15
申请人 Wuhan Kaidi Engineering Technology Research Institute Co., Ltd. 发明人 CHEN Yilong;SONG Kan;KUAI Pingyu;ZHANG Yanfeng;JIN Jiaqi
分类号 C10G2/00 主分类号 C10G2/00
代理机构 代理人
主权项 1. A method for improving Fischer-Tropsch synthesis and recycling exhaust gases therefrom, the method comprising: 1) transforming raw gas for Fischer-Tropsch synthesis using a water-gas shift reaction: CO+H2O=>CO2+H2, transporting the transformed raw gas to a Fischer-Tropsch synthesis device for Fischer-Tropsch synthesis in the presence of a Fe-based or Co-based catalyst, controlling a reaction temperature of the Fischer-Tropsch synthesis at between 150 and 300° C. and a reaction pressure of between 2 and 4 MPa (A), to yield a liquid hydrocarbon product; 2) introducing exhaust gases from the Fischer-Tropsch synthesis device to a first pressure-swing adsorber for hydrogen recovery, and controlling a purity of the hydrogen at 80-99 vol. %; 3) introducing the exhaust gases from step 2) to a second pressure-swing adsorber for methane recovery, and controlling a purity of the methane at 80-95 vol. %; 4) returning part of the hydrogen obtained from step 2) to step 1) to mix with the raw gas, and transforming a resulting mixed gas to adjust a hydrogen/carbon ratio of the raw gas for Fischer-Tropsch synthesis; and 5) introducing the methane in step 3) to a methane reforming device to reform the methane whereby yielding syngas having relatively high hydrogen/carbon ratio, transporting the syngas to step 1) to mix with the raw gas, and transforming a resulting mixed gas to adjust a hydrogen/carbon ratio of the raw gas.
地址 Wuhan CN