发明名称 Sorption process with added drying section
摘要 An adsorption process using a fractionation column including a drying section is described. The drying section dries the desorbent and removes water from the adsorption process resulting in increased capacity for the adsorbent bed.
申请公布号 US9126875(B2) 申请公布日期 2015.09.08
申请号 US201313929353 申请日期 2013.06.27
申请人 UOP LLC 发明人 Pieper Jeffrey L.;Sohn Stephen W.;Bernard Peter M.;Zimmerman Cynthia K.
分类号 C07C7/05;C07C7/00 主分类号 C07C7/05
代理机构 代理人
主权项 1. A process for the separation of a desired normal paraffin from a feed mixture comprising at least the desired normal paraffin and a non-normal paraffin comprising: passing a feed stream comprising the feed mixture through a first bed of adsorbent comprising a shape selective adsorbent and located in an adsorbent chamber which contains a plurality of compartmentalized beds of the adsorbent separated by transfer points for streams used in the process, which adsorbent selectively retains the desired normal paraffin, passing a desorbent stream into the adsorbent chamber; withdrawing an extract stream comprising the desorbent and the desired normal paraffin from the adsorbent chamber; withdrawing a raffinate stream comprising the desorbent and the non-normal paraffin from the adsorbent chamber; periodically incrementing the transfer points in the adsorbent chamber of the feed, desorbent, extract and raffinate streams to simulate countercurrent movement of the beds of adsorbent and the feed stream; separating the desired normal paraffin from the desorbent in an extract column having a separation section comprising a rectifying section and a stripping section; separating the non-normal paraffin from the desorbent in a raffinate column having a separation section comprising a rectifying section and a stripping section; passing the desorbent through a column drying section to remove water from the desorbent, the column drying section comprising a plurality of drying trays, the column drying section positioned above the rectifying section in the raffinate column, the extract column, or both; and recovering the desired normal paraffin withdrawing an overhead vapor stream comprising about 50 wt. % the desorbent from the raffinate column, the extract column, or both.
地址 Des Plaines IL US