发明名称 Conversion of hydrocarbons to carbon dioxide and electrical power
摘要 A process for the conversion of a hydrocarbon to CO2 and electrical power is described which includes subjecting a gas mixture of a hydrocarbon feed stream and steam to an integrated reforming process including stages of steam reforming in a gas-heated reformer and secondary reforming to generate a reformed gas mixture, increasing the hydrogen content of the reformed gas mixture by subjecting it to one or more water-gas-shift stages, cooling the resulting hydrogen-enriched reformed gas and separating condensed water therefrom, passing the resulting de-watered hydrogen-enriched reformed gas to one or more stages of carbon dioxide separation to recover carbon dioxide, combusting the remaining hydrogen-containing fuel stream with an oxygen containing gas in a gas turbine to generate electrical power and passing the exhaust gas mixture from the gas turbine to a heat recovery steam generation system that feeds one or more steam turbines to generate additional electrical power.
申请公布号 US9216903(B2) 申请公布日期 2015.12.22
申请号 US201013518276 申请日期 2010.11.30
申请人 Johnson Matthey PLC 发明人 McKenna Mark;Abbott Peter Edward James;Farnell Peter William
分类号 C01B3/38;F02C3/28;F01K23/06;C01B3/48;C01B3/50;C01B3/52;C01B31/20;F01K17/06;F01K23/10 主分类号 C01B3/38
代理机构 RatnerPrestia 代理人 RatnerPrestia
主权项 1. A process for the conversion of a hydrocarbon to CO2 and electrical power comprising the steps of: (i) subjecting a gas mixture comprising a hydrocarbon feed stream and steam to steam reforming by passing the mixture over a catalyst disposed in externally-heated tubes in a gas-heated reformer to form a primary reformed gas, (ii) partially combusting the primary reformed gas with a first oxygen-containing gas, and bringing the resultant partially combusted gas towards equilibrium over a secondary reforming catalyst in an autothermal reformer to form a secondary reformed gas mixture comprising hydrogen, steam and carbon oxides, (iii) passing the secondary reformed gas mixture without intermediate cooling to the gas-heated reformer to heat the tubes therein and form a partially cooled reformed gas mixture, (iv) increasing the hydrogen content of the partially cooled reformed gas mixture by subjecting it to one or more water-gas-shift stages thereby producing a hydrogen enriched reformed gas, (v) cooling the hydrogen-enriched reformed gas to below a dew point of the steam therein to condense water and separating condensed water to give a de-watered hydrogen-enriched reformed gas, (vi) passing the de-watered hydrogen-enriched reformed gas to one or more stages of carbon dioxide separation to generate a carbon dioxide stream and a hydrogen-containing fuel stream, and (vii) combusting the hydrogen-containing fuel stream with a second oxygen-containing gas in a gas turbine to generate electrical power and an exhaust gas mixture and passing the exhaust gas mixture to a heat recovery steam generation system to provide steam for one or more steam turbines and generate additional electrical power.
地址 London GB