摘要:
Described is a supported zeolite membrane that consists of a zeolite/substrate composite layer that exhibits, in the n-butane/isobutane separation, a permeance of n-butane of at least 6.10−7 mol/m2.s.Pa and a selectivity of at least 250 at the temperature of 180° C. Said zeolite/substrate composite layer is thin and continuous. This membrane is used in processes for gas separation, vapor separation and liquid separation.
摘要翻译:描述了由在正丁烷/异丁烷分离中显示正丁烷的至少6.10 -7 mol / m 2的渗透率的沸石/底物复合层组成的支撑沸石膜。 Pa,并且在180℃的温度下的选择性为至少250。所述沸石/基材复合层是薄且连续的。 该膜用于气体分离,蒸气分离和液体分离。
摘要:
Described is a process for the preparation of a supported zeolite membrane that consists of a zeolite/substrate composite layer, whose zeolite phase exhibits a crystallinity of at least 85%, comprising: a) the formation of a gel or a solution that comprises at least one source of silica and water, supplemented with at least one polar organic compound, b) bringing into contact said gel or said solution with a porous substrate, c) the crystallization of the zeolite starting from said gel or said solution; and d) the elimination of residual agents. The molar ratio of the water to the silica in the gel or the solution in stage a) is between 27:1 and 35:1. The crystallization time of stage c) is at least 25 hours.Said process is particularly suited for the preparation of zeolite membranes whose zeolite phase is of the MFI-structural type.
摘要:
The invention relates to dioctahedral phyllosilicates 2:1 whose basal spacing is at least equal to 2.0.times.10.sup.-9 m and which in the interlayer space comprise pillars based on at least one of the compounds that is selected from the group that is formed by SiO.sub.2, Al.sub.2 O.sub.3, TiO.sub.2, ZrO.sub.2, V.sub.2 O.sub.5, or any combination of the latter. Preferably, they contain fluorine. The invention also relates to a process for their preparation that includes treatment with a surfactant, followed by treatment with a primary or secondary amine and at least one alkoxide of an element that is selected from the group that is formed by the elements Si, Al, Zr, Ti and V. The invention also relates to a catalyst that comprises said phyllosilicate, at least one matrix, and optionally a zeolite Y. The invention also relates to a process for converting hydrocarbons with this catalyst, and in particular a hydrocracking process.
摘要翻译:本发明涉及基面间距至少等于2.0×10 -9 m的双八面体页硅酸盐2:1,其中在层间空间中包含基于选自由SiO 2形成的基团中的至少一种化合物的柱, Al 2 O 3,TiO 2,ZrO 2,V 2 O 5或后者的任意组合。 优选地,它们含有氟。 本发明还涉及一种其制备方法,其包括用表面活性剂处理,然后用伯胺或仲胺和至少一种选自下列元素的醇盐进行处理:元素Si,Al, Zr,Ti和V.本发明还涉及包含所述页硅酸盐,至少一种基质和任选的沸石Y的催化剂。本发明还涉及用该催化剂转化烃,特别是加氢裂化方法的方法。
摘要:
The present invention relates to stevensite or kerolite type trioctahedral phyllosilicates 2:1 containing fluorine, fluorinated in synthesis in an acid medium and modified post-synthesis to bring about Si/Al and/or Mg/Al substitutions which impart acid properties to the solid. These phyllosilicates may be incorporated in the composition of catalysts used to convert hydrocarbons, in particular for hydrocracking.
摘要:
This invention pertains to the use of a catalyst that contains at least one dioctahedral phyllosilicate 2:1, which is preferably synthesized in a fluoride medium in the presence of HF acid and/or another source of fluoride anions, whose reticulate distance is equal to at least 20×10−10 m (2 nm) and which includes pillars that are based on at least one oxide from the elements of groups IVB, VB, VIB, VIII, IB, IIB, IIA, IVA, or any combination of these oxides, and preferably selected from the group composed of SiO2, Al2O3, TiO2, ZrO2, and V2O5, or any combination of the latter and at least one element from group VIII, in a process for isomerization of a feedstock that contains mainly normal paraffins that carry 5 to 10 carbon atoms per molecule.
摘要翻译:本发明涉及使用含有至少一种双八面体页硅酸盐2:1的催化剂,其优选在HF酸和/或另一种氟化物阴离子的存在下在氟化物介质中合成,其中网状距离等于 至少20x10 -10 m(2nm),其包括基于IVB,VB,VIB,VIII,IB,IIB,IIA,IVA族元素或这些氧化物的任何组合的至少一种氧化物的柱,以及 优选选自由SiO 2,Al 2 O 3,TiO 2,ZrO 2和V 2 O 5组成的组,或者后者和来自VIII族的至少一种元素的任何组合,在主要含有主要正常链烷烃的原料异构化的方法中,其携带5至 每个分子10个碳原子。
摘要:
A process for the production of a composite membrane constituted by a continuous zeolite layer which is principally located on the surface of a glass support is described. The process comprises, in succession, at least one step in which partial hydrolysis of the silica of the internal and external surfaces of the porous support is carried out, and a zeolite crystallization step. The supported zeolite membranes obtained are advantageously used in continuous separation processes.
摘要:
A process for the production of a controlled supported zeolite membrane comprises: (a) forming a gel which is principally localised at the surface of a porous support by bringing it into contact, in succession, with two immiscible liquids which contain the agents necessary for formation of said gel, then (b) crystallising the zeolite from said gel and finally (c) eliminating the residual agents. The supported zeolite membranes obtained are advantageously used in continuous gas separation processes.