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51.
正丁烷和异丁烷在改性纳米HZSM-5上的芳构化反应 总被引:1,自引:1,他引:0
用脉冲微反装置评价了正丁烷和异丁烷在氢型和锌改性的纳米ZSM-5催化剂上的反应活性和芳构化选择性.结果表明,在550℃下,异丁烷在氢型和不同锌负载量的纳米ZSM-5催化剂上的转化率都远高于正丁烷,但其芳构化选择性低于正丁烷.脱甲基活化是异丁烷和正丁烷的重要活化方式,也是影响其芳构化选择性的主要因素.锌改性在提高异丁烷和正丁烷转化率的同时,也促进了正丁烷和异丁烷的脱甲基活化.在混合丁烷进料反应的情况下,正丁烷和异丁烷的转化率与其单独进料时十分接近,这说明正丁烷和异丁烷共存时不会发生明显的竞争吸附和反应.纳米ZSM-5因晶粒度小,孔道短和微孔扩散阻力低而有利于异丁烷转化. 相似文献
52.
Ricardo Ferreira Affeldt Rodrigo Sebastian Iglesias Fabiano Severo Rodembusch Dennis Russowsky 《Journal of Physical Organic Chemistry》2012,25(9):769-777
In this article, a series of Hantzsch 1,4‐dihydropyridines with different substituted aryl groups were synthesized and its spectral data obtained by UV–Vis absorption and fluorescence emission spectroscopies in solution. The dihydropyridines present absorption located around 350 nm and fluorescence emission in the blue–green region. A higher Stokes’ shift could be observed for the derivative 3b because of an intramolecular charge transfer in the excited state from the dimethylaniline to the dihydropyridine chromophores, which was corroborated by a linear relation of the fluorescence maxima (νmax) versus the solvent polarity function (Δf) from the Lippert–Mataga correlation. A comparison between the experimental data and time‐dependent density functional theory‐polarizable continuum model calculations of the vertical transitions was performed to help on the elucidation of the photophysics of these compounds. For these calculations, the S0 and S1 states were optimized using Becke, three‐parameter, Lee–Yang–Parr/6‐31 G* and Configuration Interaction Singles/6‐31 G*, respectively. The predicted absorption maxima are in good agreement with the experimental; however, the theoretical fluorescence emission maxima do not match the experimental, which means that the excited specie cannot be related to neither a locally excited state nor to an aromatized structure. Copyright © 2012 John Wiley & Sons, Ltd. 相似文献
53.
以HZSM-5(SiO2/Al2O3=38)为载体,偏钨酸铵为钨源制备了双功能催化剂WC/HZSM-5,考察了其催化正己烷芳构化反应性能,并采用X射线衍射、扫描电子显微镜、X射线能量散射谱和程序升温氨脱附等手段对催化剂进行了表征,探讨了制备方法和WC含量对WC/HZSM-5催化剂性能的影响.结果表明,采用原位还原碳化法制备的WC/HZSM-5(RC)催化剂上正己烷芳构化反应性能优于浸渍法制备的WC/HZSM-5(IP).5%WC/HZSM-5(RC)样品在反应初始阶段芳烃选择性为10.28%,而HZSM-5上的仅为2.56%.WC/HZSM-5(RC)催化剂上反应产物中轻质芳烃(苯、甲苯和二甲苯)含量增加,重质芳烃C9+含量降低,其催化性能优于Pt/HZSM-5催化剂.产物分布的变化可能是由于WC与分子筛间的协同作用所致. 相似文献
54.
基于76T簇模型,采用量子力学和分子力学联合的ONIOM2(B3LYP/6-31G(d,p):UFF)方法研究了H-ZSM-5分子筛上环己烯芳构化反应历程.结果表明,环己烯首先吸附在分子筛酸性位上,与酸性质子共同脱除一个H2分子后,在分子筛骨架氧上生成烷氧配合物中间体;然后再脱质子得到环己二烯,同时酸性位复原;再经历脱氢和脱质子历程,最后得到产物苯,并吸附在复原的分子筛酸性位上.计算得到脱氢的活化能依次为279.64和260.21kJ/mol,脱质子的活化能依次为74.64和59.14kJ/mol.所有脱氢反应都是吸热过程,生成表面烷氧活性中间体,随后的脱质子反应能垒较低,而且是放热过程.此外,比较了环己烯在分子筛酸性位上的三个竞争反应,即脱氢、质子化和氢交换反应的活化能垒,证明环己烯优先发生脱氢反应. 相似文献
55.
Daoke Yu Wenbin Chen Shichao Zhang Rakesh Chilivery Fuhai Li Xupeng Lu 《Phosphorus, sulfur, and silicon and the related elements》2020,195(6):464-473
AbstractThe synthesis conditions of HZSM-5 zeolite, including crystallization temperature, crystallization time and raw material ratio, were investigated by L32 (48) orthogonal test to specifically optimize its performance in dimethyl ether (DME) aromatization for the first time. Based on the total yield of aromatic products, the synthesis conditions of HZSM-5 zeolite with the best DME aromatization properties were obtained by comprehensive analysis and validation experiments. The relationship between the aromatization performance, crystalline structure, pore structure, and acidity of HZSM-5 zeolite were analyzed. The results showed that the HZSM-5 zeolite accompanied by hierarchical structure, an appropriate Brønsted and Lewis acid content and uniform crystal morphology, was successfully synthesized under optimized conditions. Over this unmodified and un-doped catalyst, the conversion of DME approached to 99.3% and the total yield of aromatics reached was 53.5%. 相似文献
56.
57.
Yi-Ping Zhang Dong-jie Wang Jin-hua Fei Xiao-ming Zheng 《Reaction Kinetics and Catalysis Letters》2001,74(1):151-161
The influence of Zn content, reaction temperature and pretreatment conditions on a Zn-modified Mo/HZSM-5 catalyst for methane
aromatization were studied. It was found that the addition of Zn promoted the reaction. Methane conversion of 10.9% and aromatics
selectivity of 96.7% were obtained with a Zn/Mo molar ratio of 0.03 and N2 pretreatment at 973 K. The results of isopropanol decomposition, NH3-TPD and TG-DTA suggest that the addition of Zn decrease the acidity of the catalyst, which may be the reason for the high
activity on the Mo-Zn/HZSM-5 catalyst.
This revised version was published online in June 2006 with corrections to the Cover Date. 相似文献
58.
甲烷无氧芳构化催化剂的活性相生成研究 总被引:3,自引:0,他引:3
利用在线质谱分析检测了在各种催化剂上甲烷的程序升温表面反应(TPSR)过程中不同物种的行为.结果表明,MoO3向Mo2C的转变阻碍了甲烷的活化及其芳构化.如果这个转变过程在TPSR反应前发生,甲烷活化和苯生成的温度将大大降低(分别为760K和847K).通过比较担载在不同分子筛上钼物种的催化行为发现,甲烷的初始活化是这个反应速率的决定步骤.只有具备合适的钼价态,Bro-nsted酸性以及特殊的分子筛孔道结构的催化剂才能使甲烷芳构化反应高效进行. 相似文献
59.
Folorunsho Aberuagba 《Reaction Kinetics and Catalysis Letters》2000,70(2):243-249
Heptene-2 aromatization on Pt/Al2O3 in a pulse microcatalytic reactor has been studied under H2 and N2 atmosphere at temperatures between 330 to 500°C and at a total pressure of 4.0 kg/cm2. Results showed that the production of only cracked products (mainly methane) from deep fragmentation of heptene-2 in H2 sharply contrasts with the reaction in N2 in which the catalyst showed aromatic selectivity with the production of methane, benzene and toluene. In H2-N2 mixtures, 75% H2 was required to reduce the aromatization activity of the catalyst to zero. A test of the kinetic data using Sica's method [15] of pulse kinetic analysis suggests a first order in heptene-2 with an activation energy of 102.61 kJ/mol in N2 and 124.71 kJ/mol in H2. The difference in activation energies has been attributed to a difference in reaction mechanisms in both gases. 相似文献
60.