发明名称 Mixed phase benzene saturation with controlled hydrogen addition
摘要 A process for saturating benzene in a stream containing hydrocarbons and benzene maintains the benzene saturation reactor in a mixed phase at specific conditions to recover a saturation reactor effluent having a low benzene concentration and a reduced temperature. The benzene saturation reactor operates in a mixed phase without a hydrogen recycle and provides a saturated benzene effluent having less than 2 mol % benzene when operated at an effluent temperature of between 480 DEG F. and 600 DEG F. The discovered temperature range is relatively high and constant for feeds containing a substantial mount of benzene, despite changes in reaction zone pressure and reaction zone liquid LHSV.
申请公布号 US5663466(A) 申请公布日期 1997.09.02
申请号 US19940351963 申请日期 1994.12.08
申请人 UOP 发明人 RICE, LYNN H.;BELL, DONALD H.
分类号 C07C5/10;C07C5/22;C10G45/52;C10G67/06;(IPC1-7):C07C5/10 主分类号 C07C5/10
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