Methanol conversion to hydrocarbons and dimethyl ether on decationized zeolite T

Methanol transformations over the hydrogen forms of zeolite T (32%–76% decationization and 13%–32% dealumination) during contact with methanol vapor was studied at 200°–400°C. The catalysts used show a high activity in methanol conversion into light hydrocarbons and dimethyl ether but over a short period.

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T (32–16% 13–32% ) 200–400°C. , .

     

n-Pentane conversion to aromatic hydrocarbons over Zn-ZSM-11 zeolite

The transformation of n-pentane into aromatic hydrocarbons over Zn-exchanged ZSM-11 zeolite (Zn-ZSM-11) has been studied. The catalyst exhibited a high activity and BTX selectivity for n-C5 conversion at about 538°C, 1 h^–1 and 1 atm. Zn-species are effective for the activation of the n-pentane and the transformation of intermediate products into aromatic compounds.

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- ZSM-11, (Zn-ZSM-11). - 538°C, 1^–1 1 . Zn - .

     

Selective ethane conversion into aromatic hydrocarbons over Zn-ZSM-11 zeolite

The conversion of ethane into aromatic compounds at 550°C and atmospheric pressure over Zn-ZSM-11 zeolite (Si/Al=17; 2.5 wt.% of Zn as counter ion) has been studied in a flow reactor at different partial pressures of ethane. The observed products at different ethane conversion levels were formed through a variety of processes including ethane dehydrogenation, producing ethylene as the only primary unstable product. Ethylene underwent very rapid reactions through carbenium ion intermediates, producing aromatic hydrocarbons and C1-C4 hydrocarbons as secondary products.     

Selective conversion of methane to aromatic hydrocarbons on large crystallite zeolite catalysts with mesoporous structure

Large crystallite mesoporous MFI (ZSM-5) zeolite was synthesized by using carbon nano-powder as a secondary template. The surface properties, morphological and phase composition of the synthesized material and of the commercial ZSM-5 (Zeolyst) zeolite were studied by nitrogen porosimetry, XRD and scanning electron microscopy. The results showed that the volume of mesopores volume increases with development of a secondary mesoporosity in the structure of zeolite. The obtained zeolite supports were used to prepare molybdenum-containing catalysts for the methane aromatization by solid phase preparation technique. Based on the XPS data, molybdenum particles in these catalysts are characterized by more uniform size distribution. The formation of a secondary pore structure restrains the carbon deposit formation as well as increases the methane conversion and the yield of the aromatic compounds.     

Ethanol conversion to aromatic hydrocarbons over several zeolite catalysts

Summary H-ZSM-5 (Si/Al₂ = 29) zeolite showed especially high activity in the conversion of ethanol to BTX (benzene, toluene, xylenes), while other zeolites exclusively formed ethylene. Noble metal catalysts supported on H-ZSM-5 (29) zeolite have high activity for the formation of BTX. Of these, Au/H-ZSM-5 catalyst can partially inhibit carbon deposition during the reaction, thus maintaining constant catalytic activity for BTX formation.     

Hydrogen production by conversion of methane over nickel-supported USY-type zeolite catalysts

Hydrogen production by conversion of methane over Ni-supported zeolite catalysts was investigated, and Ni-supported USY-type zeolite (Si/Al₂ = 14.0, 360) was found to have longer catalytic lifetime than Ni-supported silica (Cab-O-Sil) catalyst, which had been reported to have the longest catalytic lifetime for this reaction.     

Methane conversion into aromatic hydrocarbons over Ag-Mo/ZSM-5 catalysts

Nonoxidative methane conversion into aromatic hydrocarbons over ZSM-5-type high-silica zeolites modified with nanosized powders of molybdenum (4.0 wt %) and silver (0.1–0.5 wt %) is reported. The acidic properties of the catalysts have been investigated by temperature-programmed ammonia desorption. The microstructure and composition of the Ag-Mo/ZSM-5 catalytic systems have been studied by high-resolution transmission electron microscopy and energy-dispersive X-ray spectroscopy. The doping of the Mocontaining zeolite with silver enhances its activity and stability in nonoxidative methane conversion into aromatic hydrocarbons.     

负载铂催化剂中沸石载体酸性对甲烷两步转化的影响

考察了具有相同金属分散度的Pt/NaY、Pt/HNaY、 Pt/HY、Pt/NaBeta和Pt/HBeta催化剂中沸石载体的酸性对在低温下（≤250 ℃）甲烷两步等温转化反应以及由甲烷解离吸附产生的表面碳物种分布的影响。由甲烷等温两步转化生成的C2+烃类产物的总量随着载体酸性的增加而明显增加;C2～C6产物的分布也发生了变化。由表面碳物种的程序升温加氢结果表明,在各种催化剂上碳物种的形式是相似的,其总量和具有活性的Cα物种的量均因载体酸性增加而增加,反应性也增大。这种因沸石载体酸性变化而引起的载体效应是由金属和载体的相互作用造成负载在酸性载体上铂粒子的贫电子性而引起,即由金属粒子电子性质的变化而引起的催化性质的变化。     

Conversion of methanol to hydrocarbons over metal-zeolite catalysts

Ni²⁺, Cr³⁺ and Pb²⁺ exchanged CaY zeolites including mixed forms like CrNiCaY and PbNiCaY were used to study methanol conversion. The selectivity of the reaction to olefin and paraffin formation depends on the type of samples, the activation of the catalyst and the reaction conditions.

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CaY , Ni²⁺, Cr³⁺ Pb²⁺- , CrNiCaY PbNiCaY, . - , .

     

ZnCl2/NaY催化邻苯二酚与甲醇醚化反应

ZnCl2/NaY催化邻苯二酚与甲醇醚化反应;固体酸催化剂;愈创木酚     

Some peculiarities of cyclohexane conversion on zeolite catalysts

Cyclohexane conversion on zeolite and zeolite-containing catalysts has been examined. The formation of cracking, isomerization and dehydrogenation products is suggested to follow two parallel independent mechanisms through different intermediate carbocations.

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. , .

     

Selectivity of toluene disproportionation over zeolite catalysts

Three decationated zeolites (H-Y, H-ZSM-5 and H-ZSM-11) were tested in different conditions. Selectivities (to xylenes, S_x, and to para-isomer, S_p) were evaluated, together with activity, vs. time-on-stream. H-ZSM-5 proved to be the best catalyst, showing S_x1 and S_p-values larger than for the equilibrium gaseous mixture.

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(H-Y, H-ZSM-5 H-ZSM-11) . ( , S_x, , S_p) . H-ZSM-5 , S_x1 S_p, .

     

Selective acetylation of toluene to 4-methylacetophenone over zeolite catalysts

The vapour phase acetylation of toluene has been catalysed by acidic H-ZSM-5, H-mordenite and REY zeolite catalysts at 453 K in a tubular reactor at atmospheric pressure. H-ZSM-5 exhibited the best results during the reaction with respect to rate of acetylchloride conversion (TOF=7.5 mol s⁻¹ mol⁻¹ Al×10⁻⁴), conversion of acetyl chloride (60.2 wt.%) and selectivity for 4-methylacetophenone (88.3%) compared to both H-mordenite and REY zeolites. It is revealed that the activity and selectivity of the catalyst strongly depend on the acidic properties and pore openings of the zeolites, respectively. It is observed that isomer ratio (4-methylacetophenone/2-methylacetophenone) is influenced by the reaction conditions and type of zeolite used in the reaction. With increasing reaction temperature and toluene to CH₃COCl molar ratio, the conversion of CH₃COCl (ACT) increases, while it decreases with the increase in reaction time, weight hourly space velocity (WHSV), Na-content and silica to alumina molar ratio of H-ZSM-5 in the acetylation of toluene. H-ZSM-5 is deactivated under the reaction conditions.     

Direct conversion of synthesis gas to light hydrocarbons on heterogeneous catalysts

Six catalysts consisting of mixtures of catalysts for methanol synthesis and its conversion to hydrocarbons were prepared by mechanical mixing, impregnation, and coprecipitation, followed by extrusion. Phase changes occurring during various stages of preparation and after use were followed by x-ray diffraction. The catalysts were found to be nontrivial bifunctional catalysts which selectively convert synthesis gas directly to low molecular weight hydrocarbons in the range of C₁ to C₄. Methanol and dimethylether were detected as intermediates. Olefins were formed, and their further hydrogenation yielded products with high paraffinic content. Carbon dioxide retards the conversion of synthesis gas to hydrocarbons, whereas steam retards the hydrogenation of olefins. On heating the commercial zinc chromite catalyst, dehydration, reduction, and solid-state reactions occur with the formation of ZnO-ZnCr₂O₄ solid solution. Exchanging cations within the zeolite component did not affect the space lattice, but these ions tend to occupy special sites, and during service more order was detected. Copper ions tend to diffuse in ZnO, forming a solid solution, and during service metallic copper was produced.     

Rh/SiO~2和Rh/NaY催化剂上合成气反应的高压原位 红外光谱研究

采用高压原位FT-IR技术,对比研究了CO加H~2反应条件下Rh/SiO~2和Rh/NaY催化剂表面反应中间物种。在Rh/SiO~2表面上,无论在常压还是在1.0MPa合成气中,只观察到线式和桥式吸附CO。而在常压合成气中,Rh/NaY上不仅存在上述CO吸附物种,而且还有孪生型的Rh(Ⅰ)(CO)~2和少量Rh~6(CO)~1~6;当合成气压力升至1.0MPa后,Rh(Ⅰ)(CO)~2迅速转化成Rh~6(CO)~1~6和在2042cm^-^1产生吸收的单核羰基Rh物种,与此同时催化剂表面还生成了单齿和双齿乙酸根物种;这些在高压下生成的物种在合成气压力重新降回到常压时依然稳定存在。研究Rh/NaY上合成气反应表面物种与H~2的反应行为表明单齿乙酸根很可能是反应的活性中间物。这些结果说明Rh/NaY催化剂在高压合成气中的重构是诱发选择生成乙酸反应的基础。     

分子筛催化剂催化合成聚甲氧基二甲醚

以甲醇、甲缩醛和三聚甲醛为原料,考察了分子筛孔道结构、晶粒粒径、酸性及反应体系对合成聚甲氧基二甲醚反应性能的影响,并筛选出最佳反应条件。结果表明,HMCM-22分子筛具有良好的催化性能。在最佳反应条件下,以甲醇与三聚甲醛为原料,DMM2~8的选择性为65.1%;而以甲缩醛和三聚甲醛为原料,DMM2~8的选择性则达到90.6%。NH3-TPD结果表明,弱酸位有利于三聚甲醛解聚为甲醛,中强酸位促进长链分子生成,而强酸位导致DMM为主要产物。     

全氢菲在分子筛催化剂上环烷环开环反应的研究

在小型固定流化床(FFB)装置上考察了Y与ZSM-5分子筛催化剂以及Y分子筛催化剂上温度、剂油比对全氢菲裂化环烷环开环反应的影响。结果表明,全氢菲在分子筛催化剂上通过环烷环开环反应生成环己烷、十氢萘等单环或双环环烷烃;单环或双环环烷烃进一步侧链断裂生成2-甲基戊烷、甲基己烷等异构烷烃等,异构化生成二甲基环戊烷、甲乙基环戊烷等烷基环戊烷,氢转移生成苯、甲苯、二甲苯等烷基苯,进行深度氢转移反应生成萘、烷基萘等双环芳烃;另外,全氢菲也会通过脱氢缩合生成菲、芘等三环以上芳烃甚至焦炭等。由于扩散和吸附性能的影响,其裂化开环反应的选择性在Y分子筛催化剂上比在ZSM-5分子筛催化剂上高。因此,全氢菲环烷环开环与脱氢缩合反应的相对比例(s(NRO)/s(DHC))在Y分子筛催化剂上较高;在Y分子筛催化剂上,温度为475~550 ℃、剂油比为3.0~9.0,反应温度升高或者剂油比增加,双分子氢转移以及脱氢缩合反应增强,导致环烷环开环反应产物选择性降低。