首页> 外国专利> A catalyst comprising a zeolite selected from the group formed by the zeolites bare - 85, nu - 86 and nu - 87, an element of group vb and its use in hydroconversion of charges hydrocarbon

A catalyst comprising a zeolite selected from the group formed by the zeolites bare - 85, nu - 86 and nu - 87, an element of group vb and its use in hydroconversion of charges hydrocarbon

机译:包含选自由裸露的-85,nu-86和nu-87构成的沸石的沸石,vb族的元素及其在加氢烃的加氢转化中的用途

摘要

Catalyst for the hydroconversion of hydrocarbons petroleum feeds consists of a zeolite chosen from NU-85, NU-86, NU-87, optionally at least an element chosen from group VIB and group VIII, optionally at least an element from P, B, Si, and optionally an element from group VII A. An Independent claim is also included for the preparation of the catalyst carried out as follows: (a) drying and weighing of a zeolite matrix chosen from NU-85, NU-86, NU-87, optionally at least an element from group VIB and group VIII, optionally at least an element from P, B and Si, optionally at least an element from group VIIA; (b) calcining of the resulting solid from step (a) at a temperature of at least 150 deg.C; (c) impregnating the precursor solid defined in (b) by a solution of at least an element of group VB; (d) allowing the wet solid to relax under a wet atmosphere at a temperature 10-120 deg.C; (e) drying the wet solid obtained in step (b) at a temperature 60-150 deg.C The catalyst is sulfurated under a flux of a mixture of H2/H2S or under pure H2S, at a temperature 150-800 deg.C.
机译:用于烃类进料的加氢转化的催化剂由选自NU-85,NU-86,NU-87的沸石组成,任选地至少选自VIB和VIII族的元素,任选地至少选自P,B,Si的元素还包括用于制备催化剂的独立权利要求,其进行如下:(a)干燥和称重选自NU-85,NU-86,NU-87的沸石基体;任选地,至少VIB族和VIII族的元素,任选地,至少P,B和Si的元素,任选地,至少VIIA族的元素; (b)在至少150℃的温度下煅烧由步骤(a)得到的固体; (c)通过至少一种VB族元素的溶液浸渍在(b)中定义的前体固体; (d)使湿固体在10-120℃的湿气氛下松弛; (e)在60-150℃的温度下干燥步骤(b)中获得的湿固体。在H2 / H2S的混合物的熔剂中或在纯H2S下,在150-800℃的温度下将催化剂硫化。 。

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