发明名称 Process and apparatus for the production and recovery of p-xylene
摘要 A mixed aromatic stream is hydrotreated to remove olefins and fractionated to separate C9+ heavies in a distillation column reactor and the C8 and lighter material is fed to a selective adsorption unit where the para-xylene is removed. The para-xylene depleted raffinate therefrom may be subjected to isomerization to form additional para-xylene. The effluent from the isomerization can be fed to the distillation column reactor for hydrogenation of any olefins formed during the isomerization or directly to the adsorption unit.
申请公布号 US5763714(A) 申请公布日期 1998.06.09
申请号 US19970780254 申请日期 1997.01.08
申请人 CATALYTIC DISTILLATION TECHNOLOGIES 发明人 HICKEY, THOMAS P.;HEARN, DENNIS;PUTMAN, HUGH M.
分类号 B01D3/00;B01D3/16;C07C5/22;C07C7/00;C07C7/12;C07C15/08;(IPC1-7):C07C5/22;C07C7/04;C07C7/13;B01D3/34 主分类号 B01D3/00
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