发明名称 Reforming exchanger with integrated shift conversion
摘要 Reforming exchangers for syngas production are provided. The reforming exchangers can have a shell-and-tube configuration and include a shift catalyst on the shell side of the exchanger to reduce a carbon monoxide concentration in a shell side product gas mixture. Processes for forming syngas using the reforming exchangers are also provided.
申请公布号 US9126172(B2) 申请公布日期 2015.09.08
申请号 US201514691108 申请日期 2015.04.20
申请人 KELLOGG BROWN & ROOT LLC 发明人 Singh Shashi;Gursahani Kamal;Burlingame Robert;Weeks Tim;Gosnell Jim;Malhotra Avinash
分类号 C01B3/48;C01B3/26;C01B3/02;B01J8/06;C01B3/38 主分类号 C01B3/48
代理机构 代理人 Machetta Gary M.
主权项 1. A process for the production of syngas in a reforming exchanger comprising an elongated shell having a first end and a second end, wherein the process comprises: supplying a reactant feed gas to a tube side fluid inlet adjacent the second end of the reform ing exchanger; supplying a hot gas feed to a shell side fluid inlet adjacent the first end of the reforming exchanger; passing the reactant feed gas through a tube bundle comprising a plurality of tubes that contain a reforming catalyst, wherein the tubes have an inlet end secured to a tube sheet adjacent the second end of the reforming exchanger and an outlet end adjacent the shell side fluid inlet; reforming the reactant feed gas in the tubes to form a reformed product gas; discharging the reformed product gas from the tubes into the hot gas feed to form a gas mixture on the shell side of the reforming exchanger adjacent the shell side fluid inlet; passing the gas mixture from the first end of the reforming exchanger to the second end of the reforming exchanger through a catalyst bed on the shell side of the reforming exchanger, wherein the catalyst bed comprises one or more shift catalysts for selectively converting carbon monoxide in the gas mixture to carbon dioxide, forming a reduced carbon monoxide product gas mixture wherein the shift catalyst bed is in contact with the tubes outer walls, and wherein the portion of the tubes concurrent with the shift catalyst bed is void of the reforming catalyst; and recovering the reduced carbon monoxide product gas mixture from a shell side fluid outlet adjacent the second end of the reforming exchanger, wherein the shell side fluid outlet is fluidly isolated from the tube side fluid inlet by the tube sheet.
地址 Houston TX US