发明名称 |
METHOD FOR CATALYTIC REFORMING |
摘要 |
FIELD: oil processing and petrochemical industry. SUBSTANCE: benzene fractions are brought into contact at 470-520 C and at pressure 1-3 MPa, the process is carried out in the presence of platinum- and rhenium-containing catalysts being filled into 3-4 consequently disposed reactors. In the first reactor catalyst having balanced ratio of Pt and Re is used, said catalyst comprises 0.34-0.38 mass % of Pt and 0.34-0.38 mass % of Re (ratio Re/Pt being 0.89-1.12). In next reactors catalyst having non-balanced ratio of Pt and Re is used, said catalyst comprises 0.34-0.38 mass % of Pt and 0.18-0.22 mass % of Re (ratio Re/Pt being 0.47-0.64). EFFECT: increased yield of stable catalysate. 3 cli
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申请公布号 |
RU2101322(C1) |
申请公布日期 |
1998.01.10 |
申请号 |
RU19960118807 |
申请日期 |
1996.09.19 |
申请人 |
OTKRYTOE AKTSIONERNOE OBSHCHESTVO "SLAVNEFT'-JAROS;LAVNEFTEORGSINTEZ |
发明人 |
KNJAZ'KOV A.L.;ESIPKO E.A.;NIKITIN A.A.;BROJTMAN A.Z.;ZAJASHNIKOV E.N.;KHVOSTENKO N.N.;LAGUTENKO N.M.;GRIBANOV A.A.;LAZAREVA L.M.;KNJAZ'KOV A.L.;ESIPKO E.A.;NIKITIN A.A.;BROJTMAN A.Z.;ZAJASHNIKOV E.N.;KHVOSTENKO N.N.;LAGUTENKO N.M.;GRIBANOV A.A.;LAZAREVA L.M. |
分类号 |
C10G35/09;(IPC1-7):C10G35/09 |
主分类号 |
C10G35/09 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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