发明名称 Oxidative dehydrogenation of hydrocarbons to unsatd. cpds. - using catalyst carrier giving increased selectivity and yield
摘要 In the prodn. of unsatd. cpds. from paraffins, mono-olefines and/or alkyl aromatics by contact with a catalyst contg. 5-35 wt. % oxide of Mo or a carrier, at 400-700 degrees C, in presence of inert gas and/or steam, the carrier consists of (A) porous, cryst. SiO2 modified with 1-20% MgO, (B) a granulated mixt. of 50-90 wt. % MgO and 50-5% TiO2, or (C) a granulated mixt. of 70-95% MgO and 30-5% Al2o3. The exhausted catalyst is re-activated at 400-700 degrees C in a stream of gas contg. O2. Used as monomers for synthetic rubber, plastics, etc. and as raw material for organic synthesis. Absence of O2 from the reaction mixt. simplifies temp. control and reduces risk of explosion. Yield and selectivity are increased.
申请公布号 NL7900493(A) 申请公布日期 1980.07.24
申请号 NL19790000493 申请日期 1979.01.22
申请人 INSTITUT FIZIKO-ORGANICHESKOI KHIMII I UGLEKHIMII AKADEMNAUK UKRAINSKOI SSR TE KIEV, U.S.S.R. 发明人
分类号 B01J23/28;C07C5/32;C07C5/333 主分类号 B01J23/28
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