发明名称 CATALYTIC REFORMING PROCESS
摘要 petroleum processing. SUBSTANCE: hydrofined gasoline fraction is passed with recycling hydrogen-containing gas at elevated temperature and pressure through several reactors charged by platinum-containing catalyst. Gaseous product mixture is cooled, recycling hydrogen-containing gas separated in high-pressure separator, and dissolved hydrogen and C1-C3-hydrocarbons are separated in second-step separator at pressure 1.1-1.3 MPa. Instable catalysate is then stabilized in rectifier operated at top temperature 55-75 C, bottom temperature 185- 195 C, and pressure 1.1-1.3 MPa. EFFECT: increased yield of stabilized catalysate. 4 ex
申请公布号 RU2164931(C2) 申请公布日期 2001.04.10
申请号 RU19990109604 申请日期 1999.04.29
申请人 LAVNEFTEORGSINTEZ";SLAVNEFT JAROS AOOT 发明人 KHVOSTENKO N.N.;KNJAZ'KOV A.L.;LAGUTENKO N.M.;NIKITIN A.A.;ROMANOV A.A.;ANICHKIN A.A.;ESIPKO E.A.;VOLKOV N.K.
分类号 C10G61/02;C10G35/04;(IPC1-7):C10G61/02 主分类号 C10G61/02
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