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A. conversion of hydrocarbon mixtures, including the equilibrium of more concentrated c8328no aromatics;

机译:A.烃混合物的转化,包括更浓的c8328no芳烃的平衡;

摘要

Claim 1, a process for the conversion of a Hydrocarbon feed mixture comprising a larger concentration of aromatic compounds cu2088 not in balance and a Lower concentration of nonaromatic wherein the mixture is contacted with a system Dual Catalyst comprising a catalyst comprising one or both between a component of tungsteAnd at least one non zeolitic aluminosilicate and a Second Catalyst comprising 0.01 to 0.2% by mass of an elementary basis of at least one Platinum Group metal component in terms of conversion of hydrocarbons comprising a temperature of 300 to 550u00baC, pressure 100 kPa to 5 MPa and Liquid Hourly Space Velocity of 0,5 to 50 hu207bu00b9 with regard to the system of double catalyst to obtain a conversion Product comprising a reduced concentration of ETHYLBENZENE and a decrease in the concentration of non Aromatic mixture for feeding.
机译:2.根据权利要求1所述的烃进料混合物的转化方法,所述烃进料混合物包含较高浓度的不平衡的芳族化合物和较低浓度的非芳族化合物,其中所述混合物与包含催化剂的系统双重催化剂接触,所述催化剂包含一种或两种之间的催化剂。钨和至少一种非沸石铝硅酸盐和第二催化剂,其基于0.01至0.2质量%的元素基础的至少一种铂族金属组分,其转化温度为300至550℃的烃,压力关于双催化剂体系,获得100 kPa到5 MPa的液体时空速度为0.5到50 hh的时空速度,以得到转化产物,该转化产物包含降低浓度的乙基苯和非芳香族混合物浓度喂食

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