摘要:
The present invention relates to a process for the preparation of a zeolitic material having a BEA framework structure comprising the steps of: (i) providing one or more zeolitic materials having a BEA framework structure, wherein the BEA framework structure comprises YO2 and X2O3, wherein Y is a tetravalent element, and X is a trivalent element; (ii) subjecting the one or more zeolitic materials provided in step (i) to a procedure for removing at least a portion of X, preferably tetrahedrally coordinated X, from the BEA framework structure; wherein the Y:X molar ratios of the one or more zeolitic materials provided in step (i) are respectively comprised in the range of from 1 to 50.
摘要翻译:本发明涉及一种制备具有BEA骨架结构的沸石材料的方法,包括以下步骤:(i)提供一种或多种具有BEA骨架结构的沸石材料,其中BEA骨架结构包含YO 2和X 2 O 3,其中 Y是四价元素,X是三价元素; (ii)使步骤(i)中提供的一种或多种沸石材料从BEA骨架结构中除去至少一部分X,优选四面体配位的X的步骤; 其中步骤(i)中提供的一种或多种沸石材料的Y:X摩尔比分别在1至50的范围内。
摘要:
The present invention relates to a process for the alkylation of an organic compound comprising: (a) providing a catalyst comprising one or more zeolitic materials having a BEA framework structure, wherein the BEA framework structure comprises YO2 and optionally comprises X2O3, wherein Y is a tetravalent element, and X is a trivalent element, (b) contacting the catalyst with one or more alkylatable organic compounds in the presence of one or more alkylating agents in one or more reactors for obtaining one or more alkylated organic compounds, wherein the one or more zeolitic materials is obtainable from a synthetic process which does not employ an organotemplate as structure directing agent.
摘要翻译:本发明涉及一种有机化合物的烷基化方法,包括:(a)提供包含一种或多种具有BEA骨架结构的沸石材料的催化剂,其中所述BEA骨架结构包含YO 2并且任选地包含X 2 O 3,其中Y是 四价元素,X是三价元素,(b)在一个或多个烷基化剂存在下,在一个或多个烷基化剂存在下使催化剂与一种或多种可烷基化的有机化合物接触,以获得一种或多种烷基化有机化合物,其中所述一种或多种烷基化有机化合物, 更多的沸石材料可以从不使用有机模板作为结构导向剂的合成方法获得。
摘要:
The present invention relates to a process for the preparation of an isomorphously substituted RUB-36 silicate comprising (1) providing a mixture containing silica, preferably amorphous silica, and/or at least one silica precursor, water, at least one suitable structure directing agent, (2) heating the mixture obtained according to (1) under hydrothermal conditions to give a suspension containing an RUB-36 silicate, (3) separating the RUB-36 silicate, wherein (a) either the mixture according to (1) contains at least one element suitable for isomorphous substitution and/or (b) the separated RUB-36 silicate according to (3) is subjected to isomorphous substitution.
摘要:
The present invention relates to a process for the preparation of a silicate compound, comprising (1) providing at least one layered silicate; and (2) mixing said layered silicate with water and at least one silicon containing compound according to formula R4-mSi[—(SiR2)n—R]m wherein at least one residue R is a leaving group and none of the residues R contains Si; m is 0, 1, 2, 3, or 4; and n is an integer greater than or equal to 0.
摘要:
The present invention relates to a process for the preparation of a zeolitic material having a CHA framework structure, said zeolitic material comprising zeolite crystals having a core-shell structure, wherein said process comprises the steps of (1) providing a mixture comprising one or more sources for Z2O5, one or more sources for X2O3, optionally one or more structure directing agents, and seed crystals having a CHA framework structure, wherein the CHA framework structure of the seed crystals comprises YO2, X2O3, and optionally Z2O5, and wherein the seed crystals have a diameter of 450 nm or greater; (2) crystallizing the mixture provided in (1) to afford zeolite crystals comprising a core of seed crystal provided in step (1) and a shell crystallized on the seed crystal; wherein Z is a pentavalent element, Y is a tetravalent element, and X is a trivalent element.
摘要翻译:本发明涉及一种制备具有CHA骨架结构的沸石材料的方法,所述沸石材料包含具有核 - 壳结构的沸石晶体,其中所述方法包括以下步骤:(1)提供包含一种或多种 Z 2 O 5的源,X 2 O 3,任选的一种或多种结构导向剂的一种或多种来源,以及具有CHA骨架结构的晶种,其中晶种的CHA骨架结构包含YO 2,X 2 O 3和任选的Z 2 O 5,并且其中所述种子 晶体的直径为450nm以上; (2)使(1)中提供的混合物结晶,得到包含步骤(1)中提供的晶种核心的沸石晶体和在晶种上结晶的壳; 其中Z为五价元素,Y为四价元素,X为三价元素。
摘要:
Described is a process for the production of a zeolitic material having an LEV-type framework structure comprising YO2 and optionally comprising X2O3, wherein said process comprises: (1) preparing a mixture comprising one or more sources for YO2, one or more solvents, and optionally comprising seed crystals; and (2) crystallizing the mixture obtained in step (1);wherein Y is a tetravalent element, and X is a trivalent element, wherein the zeolitic material optionally comprises one or more alkali metals M, wherein the molar ratio of the total amount of the one or more solvents to the total amount of the one or more sources for YO2 based on YO2 is 9.5 or less, and wherein for crystallization temperatures of 175° C. or higher in step (2), the duration of crystallization at those temperatures is less than 14 d, as well as to a zeolitic material, preferably being obtainable or obtained according to the inventive process, said zeolitic material having an LEV-type framework structure comprising YO2 and X2O3, wherein the zeolitic material optionally comprises one or more alkali metals M, and wherein the zeolitic material displays an Y:X atomic ratio of from 1 to 9.4.
摘要翻译:描述了一种生产具有包含YO 2和任选地包含X 2 O 3的LEV型骨架结构的沸石材料的方法,其中所述方法包括:(1)制备包含一种或多种YO 2,一种或多种溶剂的来源的混合物,以及 任选地包含晶种; 和(2)使步骤(1)中获得的混合物结晶; 其中Y是四价元素,X是三价元素,其中沸石材料任选地包含一种或多种碱金属M,其中一种或多种溶剂的总量与一种或多种溶剂的总量的摩尔比 基于YO 2的YO 2的来源为9.5或更低,并且其中对于步骤(2)中的结晶温度为175℃或更高的温度,在这些温度下的结晶持续时间小于14天,以及沸石材料, 所述沸石材料具有包含YO 2和X 2 O 3的LEV型骨架结构,其中所述沸石材料任选地包含一种或多种碱金属M,并且其中所述沸石材料显示Y:X原子 比例为1〜9.4。
摘要:
Described is a process for the production of a zeolitic material having an LEV-type framework structure comprising YO2 and optionally comprising X2O3, wherein said process comprises (1) preparing a mixture comprising one or more sources for YO2, one or more solvents, and optionally comprising seed crystals; and (2) crystallizing the mixture obtained in step (1); wherein Y is a tetravalent element, and X is a trivalent element, and wherein the mixture crystallized in step (2) contains 3 wt.-% or less of one or more metals M based on 100 wt-% of YO2, preferably 1 wt.-% or less, more preferably 0.5 wt.-% or less, more preferably 0.1 wt.-% or less, more preferably 0.05 wt.-% or less, more preferably 0.01 wt.-% or less, more preferably 0.005 wt.-% or less, more preferably 0.001 wt.-% or less, more preferably 0.0005 wt.-% or less, more preferably 0.0001 wt.-% or less of one or more metals M based on 100 wt.-% of YO2, wherein even more preferably the mixture crystallized in step (2) contains no metal M, wherein M stands for sodium or potassium, preferably for sodium and potassium, more preferably for the group of alkali metals, wherein even more preferably M stands for the group of alkali and alkaline earth metals.
摘要:
The present invention relates to a process for preparing at least one sheet silicate comprising Ga and/or Zn, and based thereon, a framework silicate, preferably of the RRO structure type, to the sheet silicate and framework silicate themselves and to the uses of the silicates, especially of the framework silicate, preferably as catalysts.
摘要:
The invention relates to a method for the hydrothermal production of a microporous membrane. According to said method, a colloidal solution comprising zeolite frameworks with 4-ring, 6-ring, and/or 8-ring pores which are provided as crystallites whose size ranges from 2 to 25 nm is applied to a porous substrate with the aid of a wet application technique. The applied layer is contacted with a hydrothermal liquid, and a nanocrystalline, microporous zeolite layer having an average pore diameter of 0.2 to 0.45 nm is synthesized at temperatures ranging between 50 and 250° C. and at an autogenous pressure. Such a microporous membrane comprising a porous substrate and at least one nanocrystalline zeolite layer that is disposed thereupon and has an average pore diameter of 0.2 to 0.45 nm is advantageously suitable for use as a separating device for gas phase separation, making it possible to separate particularly N2O2, N2/CO2, H2/CO2, or CO2/CH4 gas mixtures. Said separating device is especially temperature-resistant and can therefore be integrated directly into thermal processes.