Ga改性ZSM-5分子筛催化丙烷芳构化性能研究

用离子交换法制备Ga改性ZSM-5双功能催化剂,并结合XRD、SEM、BET、NH₃-TPD、Py-IR及ICP、XPS等多种技术进行表征,考察分子筛硅铝比(Si/Al)和催化剂氧化还原预处理条件对分子筛的酸性质、Ga物种的存在状态及其丙烷芳构化催化性能的影响。研究表明,硅铝比不仅可以改变分子筛的酸性,也会影响分子筛中非骨架Ga物种与分子筛表面的相互作用程度,进而影响含Ga分子筛的丙烷芳构化性能。在质量空速1.0 h^-1、反应温度550℃ 下,Si/Al比为30的Ga-HZSM-5分子筛丙烷转化率和芳烃收率最高。Ga物种的引入可以提高丙烷的转化率和芳烃的选择性,并抑制烷烃、烯烃的裂解。H₂还原处理,将分子筛表面Ga₂O₃还原为低价的Ga⁺和GaH⁺₂物种,促进了Ga物种向分子筛微孔迁移;还原-氧化处理后,Ga⁺和GaH⁺₂物种氧化成GaO⁺,占据分子筛孔道离子交换位,显著提高了催化剂的芳构化活性。     

原位固体核磁共振研究温和条件下丙烷在镓改性H-ZSM-5上的活化

将价格低廉、储量丰富的低碳烷烃 ( C1～C5)转化为高附加值的工业产品是多相催化研究中的一个重要领域[1～ 6 ] .镓改性的 H-ZSM-5催化剂已被广泛应用于丙烷芳构化的工业化生产中[7,8] .然而 ,由于低碳烷烃中碳碳和碳氢键的高稳定性 ,低碳烷烃的转化通常需要较高的反应温度 ,因     

The initial stages of solid acid-catalyzed reactions of adsorbed propane. A mechanistic study by in situ MAS NMR

In situ solid-state NMR spectroscopy was employed to study the kinetics of hydrogen/deuterium exchange and scrambling as well as (13)C scrambling reactions of labeled propane over Al(2)O(3)-promoted sulfated zirconia (SZA) catalyst under mild conditions (30-102 degrees C). Three competitive pathways of isotope redistribution were observed during the course of the reaction: (1) a regioselective H/D exchange between acidic protons of the solid surface and the deuterons of the methyl group of propane-1,1,1,3,3,3-d(6), monitored by in situ (1)H MAS NMR; (2) an intramolecular H/D scrambling between methyl deuterons and protons of the methylene group, without exchange with the catalyst surface, monitored by in situ (2)H MAS NMR; (3) a intramolecular (13)C scrambling, by skeletal rearrangement process, favored at higher temperatures, monitored by in situ (13)C MAS NMR. The activation energy of (13)C scrambling was estimated to be very close to that of (2)H scrambling, suggesting that these two processes imply a common transition state, responsible for both vicinal hydride migration and protonated cyclopropane formation. All pathways are consistent with a classical carbenium ion-type mechanism.     

Influence of lead on propane aromatization over Pt/ZSM5 catalysts

Aromatization of propane has been investigated over Pt-Pb/ZSM5. Addition of Pb decreases propane conversion with a corresponding increase in the aromatic selectivity. Hydrogenolysis reactions are inhibited by the presence of lead.

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Pt–Pb/ZSM-5. Pb . .

     

Oxidative dehydrogenation of propane over Ni-Mo-Mg-O catalysts

In this work, a series of Ni-Mo-Mg-O catalysts with mesoporous structure prepared by sol-gel method were investigated for the oxidative dehydrogenation of propane (ODHP). The techniques of temperature-programmed reduction with H2 (H2-TPR), N2 adsorption-desorption, Fourier transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD) and X-ray photoelectron spectra (XPS) were employed for catalyst characterization. It is found that the activity of the catalysts for ODHP increases first and then decreases with the increase of Mo content. The catalyst with a Mo/Ni atomic ratio of 1/1 exhibits the best catalytic activity, which gives the propene selectivity of 81.4% at a propane conversion of 11.3% under 600°C and maintains the good catalytic performance for 22 h on stream. This is related not only to its high reducibility and dispersion as revealed by TPR and XRD, but also to the formation of more selective oxygen species on the MoOx-NiO interface as identified by XPS.     

Aromatization of methane by using propane as co-reactant over cobalt and zinc-impregnated HZSM-5 catalysts

The activities of the cobalt and zinc-impregnated HZSM-5 catalysts to the non-oxidative conversion of propane (C3) and methane (C1) into aromatic hydrocarbons were evaluated using a fixed-bed microreactor. C1 conversion reached 36.7% and the selectivity of aromatic products reached above 88.7% at atmospheric pressure, weight (hourly) space velocity (WHSV) 1.6 g h⁻¹/(g cat)⁻¹ and 873 K. The influence of the acidity and the ratio of cobalt in the catalyst on the conversion of methane and propane was evaluated. C1 incorporation was conclusively confirmed by the mass spectral analyses of aromatic products produced in a run with ¹³CH₄ which shows a significant ¹³C enrichment in the C₆H₆⁺, C₇H₈⁺ and C₈H₁₀⁺ fragments. The methane activation could result from its hydrogen-transfer reaction with alkenes. These catalysts were thoroughly characterized using XRD, N₂ adsorption measurements, TPD of NH₃, and FT-IR. The results showed that the activation of methane in low temperature was due to existence of propane. The acidic changes and micropore area of the catalyst severely affected aromatization, and resulted in drastic modifications in product distribution. From this work, we found that only a small fraction of tetrahedral framework aluminum, which corresponds to the Bronsted acid sites, is sufficient to accomplish the aromatization of the intermediates in methane and propane aromatic reaction, while the superfluous strong Bronsted acid sites, which can be decreased by adding Co and Zn, are showed to be related with the aromatic carbonaceous deposits on the catalysts. The density of acidic site and the strength of strong acid decreased when the concentration of Co and Zn in the catalyst increased. Therefore, a much higher benzene yield and a longer durability of the catalysts are obtained when compared with the conventional HZSM-5 catalysts.     

杂多化合物催化丙烷的选择性氧化

杂多化合物由杂多阴离子和阳离子组成,杂多阴离子具有一定的空间结构,多种不同结合强度的晶格氧能够在氧化-还原反应中起传递电子和氧的作用。杂多化合物具有很强的酸性,可用作双功能催化剂。本文以磷、钼、钒杂多酸中掺杂过渡金属离子Cs^2 、Cu^2 、Fe^3 为催化剂,对丙烷氧化反应进行了研究。     

丁烯在纳米H-ZSM-5催化剂上的催化裂解反应

在小型固定床反应器中考察了纳米H-ZSM-5催化剂(晶粒度为20～50nm)对丁烯催化裂解制丙烯反应的催化性能,并与两种微米H-ZSM-5催化剂样品(晶粒度分别为1～2和1～6μm)进行了比较.结果表明,在相同的反应条件下,纳米H-ZSM-5和微米H-ZSM-5催化剂上的初始丁烯转化率及丙烯收率相当,但纳米H-ZSM-5催化剂在反应中的抗积碳失活性能优于微米H-ZSM-5催化剂.在进料质量空速7h-1,常压和560℃的条件下反应,当丁烯转化率和丙烯收率下降50%时,两种微米催化剂上的反应时间仅为28h左右,而纳米催化剂上的反应时间为120h左右.积碳分析结果表明,纳米催化剂上的积碳速率明显低于微米催化剂.     

H MAS NMR monitoring of the C-labeled carbon scrambling for propane in zeolite H-ZSM-5

It has been demonstrated that ¹H MAS NMR spectroscopy can be used as a tool for in situ monitoring the reaction kinetics of ¹³C-labeled carbon scrambling in alkane molecules adsorbed on zeolite catalysts at the reaction temperature of 540–570 K. The accuracy of the results and the time resolution are improved compared to ¹³C MAS NMR spectroscopy.     

Zn/H-ZSM-5催化剂上的二甲醚芳构化反应

 考察了 H-ZSM-5 和 Zn/H-ZSM-5 催化剂的二甲醚芳构化性能. 结果表明, H-ZSM-5 分子筛催化剂酸性的增强和酸中心的增多有利于二甲醚芳构化. 当在 H-ZSM-5 催化剂中加入 2% Zn 时, 在 360 oC 下反应时总芳烃收率从 50.0% 增加至 66.2%, C8 芳烃收率从 28.6% 增加到 39.0%. 反应温度升高到 480 oC 时, 总芳烃收率增加至 78.0%.     

Dehydrogenation of propane in the presence of carbon dioxide over oxide-based catalysts

In the present study, we show the advantages of CO₂ use for the dehydrogenation of propane to propene on the basis of thermodynamic considerations and some experimental results. Several metal oxides Ga₂O₃, Cr₂O₃, Fe₂O₃ unsupported and supported on g- Al₂O₃ and SiO₂ were tested. Ga₂O₃ catalyst was found to be an effective agent for dehydrogenation of propane to propene. The yield of propene at 873 K was 30.1 %. This revised version was published online in June 2006 with corrections to the Cover Date.     

Palladium species in Pd/H-ZSM-5 zeolite catalysts for CH4-SCR

The active state of palladium for NO reduction with methane (CH₄-SCR) was investigated by comparing the catalytic activity of Pd/H-ZSM-5 with that of PdO/SiO₂. High catalytic activity for CH₄-SCR was given by Pd/H-ZSM-5 in the temperature range of 300–500 °C. PdO/SiO₂ catalyzed the reaction between NO₂ and CH₄ in the absence of oxygen, which retarded the reaction by consuming CH₄ in combustion. CH₄ combustion occurred on either zeolite-supported or silica-supported catalyst, while NO preferentially retarded the combustion on Pd/H-ZSM-5. NO was found to be chemisorbed on the palladium sites in zeolite, while it was hardly chemisorbed on PdO/SiO₂. NaCl titration showed that the palladium species in zeolite are Pd²⁺ cations content, on which NO is strongly chemisorbed resulting in high selectivity for CH₄-SCR.     

Studies on the conversion of isopentane over shape selective zeolites, I. H-ZSM-5 and H-ZSM-11 zeolites

H-ZSM-5 and H-ZSM-11 efficiently catalyze the conversion of isopentane into aromatic hydrocarbons.n-Pentane produces more aromatic hydrocarbons than isopentane, but at low conversion levels (high space velocity) isopentane was about two times more reactive thann-pentane in terms of the first order rate constant for the cracking of the pentane isomers.     

苯和甲醇在H-ZSM-5催化剂上甲基化的反应机理

采用our own-N-layered integrated molecular orbital+molecular mechanics(ONIOM)和密度泛函理论(DFT)结合的方法,在5T、12T、104T_9和104T_(12)H-ZSM-5模型中研究了苯和甲醇甲基化的分步和协同机理。描述了中间体物种和过渡态的结构。考察了H-ZSM-5催化剂Br?nsted(B)酸强度对苯和甲醇甲基化反应机理的影响。反应活化能结果表明,在B酸强度更强的H-ZSM-5催化剂上,苯和甲醇甲基化反应更容易发生,反应活化能更低。随着B酸强度增强,分步机理的反应活化能比协同机理的反应活化能降低的更多。B酸强度增强对分步机理更有利。当分步机理成为主导反应路径时,分步机理中甲醇脱水步骤生成的甲氧基中间体进一步生成大体积烃类的副反应会导致H-ZSM-5催化剂因积炭而失活。合理调变H-ZSM-5催化剂的酸强度对提高催化剂的催化活性和稳定性有重要意义。     

Selective oxidation of propane to acrylic acid over mixed metal oxide catalysts

The effects of metal atomic ratio, water content, oxygen content, and calcination temperature on the catalytic performances of MoVTeNbO mixed oxide catalyst system for the selective oxidation of propane to acrylic acid have been investigated and discussed. Among the catalysts studied, it was found that the MoVTeNbO catalyst calcined at a temperature of 600 ℃ showed the best performance in terms of propane conversion and selectivity for acrylic acid under an atmosphere of nitrogen. An effective MoVTeNbO oxide catalyst for propane selective oxidation to acrylic acid was obtained with a combination of a preferred metal atomic ratio （Mo1V0.31Te0.23Nb0.12）. The optimum reaction condition for the selective oxidation of propane was the molar ratio of C3H8 ：O2 ： H2O ： N2 = 4.4： 12.8 ： 15.3 ： 36.9. Under such conditions, the conversion of propane and the maximum yield of acrylic acid reached about 50% and 21%, respectively.     

Studies on the oxidative dehydrogenation of propane to propene over Co-V-O catalysts

A series of Co-V-O catalysts were prepared and their catalytic performances for the oxidative dehydrogenation of propane to propene were investigated. It was found that the p-type catalysts showed higher catalytic behavior than the n-type catalyst.     

In-situ FTIR studies of dimethyl ether adsorption on H-ZSM-5 zeolites

In situ infrared spectra of dimethyl ether adsorbed on two H-ZSM-5 zeolites are reported which are different in both lattice and extraframework aluminium contents. A number of dissociatively adsorbed dimethyl ether species associated respectively with the Bronsted acid sites, the external silanol groups and extraframework aluminium species at different temperatures are identified. In particular, dimethyl ether reacts with non acidic hydroxyl species associated with extraframework aluminium to form the third methoxy species. The distributions of hydrocarbons desorbed from a single pulse of dimethyl ether (1.0 mL) onto these zeolite samples are presented. Propene is the major product, and the yield of hydrocarbons correlates with the concentration of Bronsted acid bound methoxy groups.     

H-ZSM-5分子筛上苯与乙醇和乙烯烷基化反应的理论研究

采用ONIOM2(B3LYP/6-31G(d):UFF)计算方法研究了H-ZSM-5分子筛上苯与乙醇和乙烯烷基化反应历程.选取40T簇模型模拟了H-ZSM-5分子筛位于孔道交叉点的酸性位.从生成能和反应活化能角度分析并比较了苯与乙醇和乙烯烷基化反应机理.结果表明,苯与乙醇的烷基化按照分步机理进行,速控步骤的活化能为170.34 kJ/mol.而乙烯作为烷基化剂与苯反应时同时存在联合机理和分步机理,且二者之间存在一定程度的竞争,其中联合机理的活化能为167.24 kJ/mol,分步机理速控步骤的活化能为155.20 kJ/mol.比较苯与乙醇和乙烯发生烷基化反应的机理可以看出,二者作为烷基化试剂对烷基化反应性能影响不大.     

Influence of catalyst binder on the acidity and activity/selectivity of Ga/H-ZSM-5 zeolite in propane aromatization

The acidity and initial and time-on-stream activity in propane aromatization (at 550°C, space velocity of 3100 cm³g⁻¹ _(zeolite)h⁻¹) of Ga-impregnated H-ZSM-5 zeolite without or with binders (50 wt%), such as silica, alumina and kaolin, have been investigated. Both the acidity and catalytic activity of the zeolite are influenced by the presence of binder in the catalyst, depending upon the binder. The influence is found to be lowest for alumina and highest for kaolin. Among the binders, alumina is the most preferred binder for the zeolite catalyst.     

Selective reduction of nitric oxide with methane on In/H-ZSM-5-based catalysts

There have been many studies on the catalysis of selective catalytic reduction of nitric oxide with hydrocarbons. It was shown in our previous works that Ir/In/H-ZSM-5 has high catalytic activity and selectivity for this reaction by use of methane as a reductant. The reaction of CH4 -SCR proceeds consecutively as NO oxidation to NO2 and NO2 reduction with CH4 . These two reactions take place bifunctionally on different kinds of catalytic sites: NO oxidation on Ir and NO 2 reduction on InO+ sites. The studies of NOx chemisorption and kinetics of NOx reduction with CH4 lead us to conclude that the bifunctional catalysis is remarkably facilitated by the coexistence of these sites in the identical pores of zeolite, which may be called "intrapore catalysis". In this review, the design of highly active and selective catalysts for this reaction system will be discussed on the basis of bifunctionality.