摘要:
A process for oligomerizing isobutene includes contacting a feedstock including isobutene with a catalyst comprising an EMM-10 molecular sieve under conditions effective to oligomerize said isobutene and produce an effluent containing less isobutene than the feedstock.
摘要:
A method of making a crystalline molecular sieve of MFS framework type, said method comprising the steps of (a) adding at least one source of ions of tetravalent element (Y), at least one source of ions of trivalent element (X), at least one hydroxide source (OH−), at least one structure-directing-agent (R), at least one seed source (Seed), and water (H2O) to form a mixture having the following mole composition (expressed in term of oxide): YO2:(n)X2O3:(x)OH−:(y)R:(z)H2O+(m)Seed wherein the m is in the range of from about 10 wtppm to about 2 wt. % (based on total weight of the synthesis mixture), the n is in the range of from about 0.005 to 0.05, the x is in the range of from about 0.01 to about 0.3, the y is in the range of from about 0.03 to about 2; and the z is in the range of from about 3 to about 30; and (b) treating said mixture under crystallization conditions to form said crystalline molecular sieve substantially free of non-MFS material, wherein said crystallization conditions comprise a temperature in the range of from about 150° C. to about 250° C., and crystallization time less than 100 hr, the weight hourly throughput is at least 0.001 hr−1.
摘要翻译:一种制备MFS框架型结晶分子筛的方法,所述方法包括以下步骤:(a)将至少一种四价元素(Y)的离子的至少一种源,至少一种三价元素(X)的离子源加入 至少一种氢氧化物源(OH - ),至少一种结构导向剂(R),至少一种种子源(Seed)和水(H 2 O 2) )以形成具有以下摩尔组成(以氧化物表示)的混合物:<?in-line-formula description =“In-line Formulas”end =“lead”?> YO 2: (n)X 2 O 3(x)OH - (y)R:(z)H 2 SUB> O +(m)种子<?in-line-formula description =“In-line Formulas”end =“tail”?>其中m在约10重量ppm至约2重量%的范围内。 %(基于合成混合物的总重量),n在约0.005至0.05的范围内,x在约0.01至约0.3的范围内,y在约0.03至 约2; 并且z在约3至约30的范围内; 和(b)在结晶条件下处理所述混合物以形成基本上不含非MFS材料的所述结晶分子筛,其中所述结晶条件包括在约150℃至约250℃范围内的温度和结晶 时间小于100小时,重量小时生产量至少为0.001小时-1。
摘要:
A method of crystallizing a crystalline molecular sieve having a pore size in the range of from about 2 to about 19 Å, said method comprising the steps of (a) providing a mixture comprising at least one source of ions of tetravalent element (Y), at least one hydroxide source (OH−), and water, said mixture having a solid-content in the range of from about 15 wt. % to about 50 wt. %; and (b) treating said mixture to form the desired crystalline molecular sieve with stirring at crystallization conditions sufficient to obtain a weight hourly throughput from about 0.005 to about 1 hr−1, wherein said crystallization conditions comprise a temperature in the range of from about 200° C. to about 500° C. and a crystallization time less than 100 hr.
摘要:
A method for increasing the efficiency of xylene isomerization by using a two stage isomerization process. In the first stage of the process, a C.sub.9.sup.+ aromatics feedstock is subjected to ethylbenzene conversion and xylene isomerization. Non-C.sub.8 aromatics are removed from the effluent, which is then processed in a second stage of the process to remove para-xylene and isomerize the para-xylene depleted effluent. The effluent from the second stage isomerization unit is then recycled into the inlet of the second stage of the process and a slip stream from the para-xylene separator is recycled to the feedstock and to the effluent of the ethylbenzene conversion unit. In this way, the production of para-xylene is maximized. In a preferred embodiment, toluene is co-fed into the feedstock to minimize the loss of xylenes during the ethylbenzene conversion reaction.
摘要:
There is provided a continuous toluene disproportionation process to selectively produce para-xylene. The process includes a steady-state of operation, wherein the conversion of toluene and selectivity to para-xylene is maintained at essentially constant target levels. Prior to such a steady-state of operation, the reaction is conducted under a relatively high temperature.
摘要:
A process is provided for alkylating an isoparaffin with an olefin comprising effecting reaction of isoparaffin and olefin in the presence of an alkylation catalyst complex comprising a Lewis acid and a solid component, said solid component comprising a layered silicate and pillars of an oxide of at least one element selected from Groups IB, IIB, IIIA, IIIB, IVA, IVB, VA, VB, VIA, VIIA and VIIIA of the Periodic Table of the Elements separating the layers of the silicate.
摘要:
Pillared layered silicate compositions containing pillars of silica and metal oxides, e.g., alumina are prepared by contacting organic-swelled layered silicates, e.g. kenyaite-type materials, with a hydrolyzable silica precursor, e.g., tetraethylorthosilicate which forms silanol groups between the layers and contacting the resulting product with an aqueous solution containing inorganic metal salt and effecting hydrolysis of the silanol groups.
摘要:
There is provided layered oxides of aluminum and phosphorus or arsenic having pendant organic groups which protrude into the inner layer region of these layered materials. These materials may be prepared by reacting a suitable organoarsenic or organophosphorus compound, such as phenylphosphonic acid, with a suitable aluminum compound, such as alumina, in the presence of a suitable solvent, such as a mixture of ethanol and water, under conditions of elevated temperature.
摘要:
There is provided a process for the dehydrogenation of saturated hydrocarbons having from 2 to 5 carbon atoms. The feed is contacted with a catalyst which includes a base metal or noble metal which is incorporated into or onto a pillared layered silicate. A preferred pillared layered silicate is kenyaite containing interspathic silica, and a preferred base metal or noble metal is chromium.