发明名称 Process for CO<sub>2 </sub>capture with improved stripper performance
摘要 The present application relates to systems and processes for removal of gaseous contaminants from gas streams. In particular, the application relates to a process for removal of gaseous contaminants from a gas stream comprising contacting the gas stream with a wash solution to remove gaseous contaminants from the gas stream by absorption into the wash solution; andregenerating the used wash solution to remove gaseous contaminants from the used wash solution, to provide a regenerated wash solution and a gas comprising removed contaminants,wherein in a first regeneration stage the gas comprising removed contaminants is cooled to minimize loss of water vapor from the regeneration step.
申请公布号 US8845789(B2) 申请公布日期 2014.09.30
申请号 US201012732961 申请日期 2010.03.26
申请人 ALSTOM Technology Ltd 发明人 Baburao Barath;Leister Jonathan W.;Vitse Frederic
分类号 B01D53/14 主分类号 B01D53/14
代理机构 代理人 Flanigan Cynthia W.
主权项 1. A process for removal of gaseous contaminants from a gas stream, comprising a) contacting a gas stream comprising gaseous contaminants with a wash solution, to remove gaseous contaminants from the gas stream by absorption into the wash solution; b) passing used wash solution resulting from step a) to regeneration; c) regenerating used wash solution by removal of gaseous contaminants from the wash solution, to provide a regenerated wash solution and a gas comprising removed contaminants; d) passing the regenerated wash solution to reboiling; e) reboiling the regenerated wash solution for further removal of gaseous contaminants from the wash solution, to provide a reboiled wash solution; f) returning the reboiled wash solution to step a); wherein during step f), the returned reboiler wash solution is subjected to heat-exchanging with the regenerated wash solution of step d) in a first heat-exchanging step, to heat the regenerated wash solution; andheat-exchanging with used wash solution of step b) in a second heat-exchanging step, to heat the used wash solution; and further comprisingwithdrawing a first portion of used wash solution resulting from the second heat-exchanging step; andbetween the first and second heat-exchanging steps, subjecting the returned reboiler wash solution to heat-exchanging with the withdrawn portion of used wash solution in a third heat-exchanging step, to heat the used wash solution.
地址 Baden CH