Use of an omega zeolite based catalyst comprising at least one metal
from groups IIa, IVb, IIb or IVa for the dismutation and/or
transalkylation of alkylaromatic hydrocarbons
    41.
    发明授权
    Use of an omega zeolite based catalyst comprising at least one metal from groups IIa, IVb, IIb or IVa for the dismutation and/or transalkylation of alkylaromatic hydrocarbons 失效
    使用包含至少一种IIa,IVb,IIb或IVa族金属的基于ω-沸石的催化剂用于烷基芳族烃的歧化和/或烷基转移

    公开(公告)号:US5773678A

    公开(公告)日:1998-06-30

    申请号:US796188

    申请日:1997-02-07

    摘要: The invention concerns the use of a catalyst comprising at least one zeolite having a mazzite type structure in its acid form, the catalytic properties of the catalyst having been modified by depositing, on the external surface of the crystals, at least one metal selected from metals from group IIa of the periodic classification of the elements, such as Be, Mg, Ca, Sr or Ba, group IVb, such as Ti, Zr or Hf, group IIb such as Zn, Cd or Hg and group IVa such as Ge, Sn or Pb, said catalyst also comprising at least one matrix and, optionally at least one element selected from the group formed by IB and VIII of the periodic classification of the elements, for the dismutation of alkylaromatic hydrocarbons, preferably for the dismutation of toluene to produce benzene and xylenes, and/or for the transalkylation of alkylaromatic hydrocarbons, preferably for the transalkylation of toluene and trimethylbenzenes to produce xylenes.

    摘要翻译: 本发明涉及使用包含至少一种具有酸性形式的具有尖晶石型结构的沸石的催化剂,催化剂的催化性质通过在晶体的外表面上沉积至少一种选自金属的金属进行改性 来自元素周期性分类的组IIa,例如Be,Mg,Ca,Sr或Ba,IVb族,如Ti,Zr或Hf,IIb族如Zn,Cd或Hg,Ⅳa如Ge, Sn或Pb,所述催化剂还包含至少一种基质和任选的至少一种选自元素周期性分类的IB和VIII形成的基团,用于歧化烷基芳族烃,优选用于甲苯歧化 产生苯和二甲苯,和/或用于烷基芳烃的烷基转移,优选用于甲苯和三甲基苯的烷基转移以产生二甲苯。

    Method of producing liquid hydrocarbons from natural gas, in the
presence of a catalyst based on zeolite and gallium
    42.
    发明授权
    Method of producing liquid hydrocarbons from natural gas, in the presence of a catalyst based on zeolite and gallium 失效
    在基于沸石和镓的催化剂存在下,从天然气生产液态烃的方法

    公开(公告)号:US5288935A

    公开(公告)日:1994-02-22

    申请号:US886226

    申请日:1992-05-21

    摘要: The invention concerns a method of producing liquid hydrocarbons from natural gas, characterized in that:a) the natural gas is separated in (2) into at least two fractions, a first fraction of gas enriched with methane and a second fraction enriched with C2+ alkanesb) the methane is selectively oxidised in (7a) by molecular oxygen in the presence of a catalyst for oxidizing linkage of methanec) the fraction enriched with C2+ alkanes is at least partly mixed with the effluent from selective oxidation, when at least 80% of the molecular oxygen introduced at stage (b) has already been consumed at stage (b)d) the mixture resulting from stage (c) is pyrolysed in (7b)e) when the temperature of the mixture from stage (d) has been brought to a temperature from 300.degree. to 750.degree. C. and more particularly from 420.degree. to 550.degree. C., at least part of the olefins is converted to aromatics in (11c), in the presence of a special catalyst containing a zeolite, gallium, one or more Group VIII metals and/or rhenium, one or more additional metals selected from tin, lead, indium, germanium and thallium, possibly an alkali metal or alkaline earth metal and possibly a matrix.

    摘要翻译: 本发明涉及从天然气生产液体烃的方法,其特征在于:a)将天然气在(2)中分离成至少两个馏分,富含甲烷的第一部分气体和富含C2 +烷烃的第二馏分 b)在用于氧化甲烷连接的催化剂的存在下,通过分子氧在(7a)中甲烷被选择性氧化c)富含C 2 +烷烃的级分至少部分地与来自选择性氧化的流出物混合,当至少80% 在步骤(b)中引入的分子氧已经在阶​​段(b)d被消耗)d)当从步骤(d)得到的混合物的温度已经 使温度从300摄氏度到750摄氏度,更特别是从420摄氏度到550摄氏度,在含有沸石的特殊催化剂的存在下,至少部分烯烃转化为(11c)中的芳族化合物, 镓,一种或一种 Ⅷ族金属和/或铼,选自锡,铅,铟,锗和铊中的一种或多种另外的金属,可能是碱金属或碱土金属以及可能的基质。