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Catalytic conversion and thermal dealkylation of alkyl aromatics - using the same reactor and catalyst

机译:烷基芳烃的催化转化和热脱烷基-使用相同的反应器和催化剂

摘要

Combined single reactor process is for (A) catalytic conversion (e.g. trans-alkylation) of 7-12C alkyl aromatic hydrocarbons, or alternatively (B) thermal hydro-dealkylation of the same hydrocarbons, on an acid heterogeneous catalyst. (A) is carried out at 288-538 degrees, and (B) at 427-704 degrees C with addn. to the charge of an agent for reversible poisoning of the acid sites on the catalyst. The catalyst is a crystalline Al silicate zeolite material or thermal decomposition product thereof. The poisoning agent is a basic cpd. contg. S, N or O atoms. Reactor is used for disproportionation of toluene to benzene, isomerisation etc. A single reactor system can be used for both processes the change-over being effected by stopping or starting the flow of poisoning agent and charging the operating conditions.
机译:组合的单反应器方法是用于(A)7-12C烷基芳族烃的催化转化(例如,烷基转移),或(B)在酸多相催化剂上将相同的烃进行热加氢脱烷基。 (A)在288-538度下进行,(B)在427-704℃下进行加成。用于使催化剂上酸性位点可逆中毒的试剂。该催化剂是结晶硅酸铝沸石材料或其热分解产物。中毒剂是基本的cpd。续S,N或O原子。反应器用于甲苯向苯的歧化,异构化等。单个反应器系统可用于两个过程,即通过停止或开始中毒剂的流动以及补充操作条件来实现转换。

著录项

  • 公开/公告号IT1054955B

    专利类型

  • 公开/公告日1981-11-30

    原文格式PDF

  • 申请/专利权人 MOBIL OIL CORP;

    申请/专利号IT19760019299

  • 发明设计人

    申请日1976-01-15

  • 分类号C10G;

  • 国家 IT

  • 入库时间 2022-08-22 13:30:29

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