在Mo-Bi-Ce/SiO_2催化剂上内扩散对甲醇氧化制甲醛Redox机理动力学的影响

在30—40目的Mo-Bi-Ce/SiO_2催化剂上,甲醇氧化制甲醛反应在动力学区域进行时,其动力学服从Redox 机理方程。当催化剂颗粒增大至2mm 时,内扩散对甲醇氧化制甲醛的反应影响严重,催化剂的有效因子在0.47—0.85之间,从Redox 机理方程出发,对此值进行了内扩散影响的理论分析。内扩散对Redox 机理方程的反应活化能的影响服从(15)式,并从实验上得到证实。用动力学方法测定了甲醇的扩散系数。     

在铜锰铁氧化物催化剂上乙醇部分氧化反应动力学研究

研究了乙醇在铜锰铁氧化物催化剂上的部分氧化反应,包含产物乙醛阻抑作用在内的三步骤Redox机理动力学方程能较好地描述此反应的过程。考察了乙醛的阻抑机理,计算了催化剂还原步骤和再氧化步骤的活化能,并提出了当乙醛分压较低时的简化动力学方程。     

Mo-Ce/SiO2催化剂上甲醇氧化制甲醛的催化剂的有效因子及甲醇的压力分布

在Mo-Ce/SiO₂催化剂上甲醇氧化制甲醛的动力学方程可表达为甲醇及甲醛吸附的Redox机理方程,当催化剂颗粒直径增大到3mm时,内扩散强烈地影响反应速度。催化剂有效因子η可用一般速度方程的近似方法进行解释。催化剂孔内甲醇的压力分布可用下式求得:(这里有图片19900813-843-1.GIF)     

银催化剂上丁二烯环氧化宏观反应动力学的研究

考察了在Ba-Cs-Cl-Ag/α-Al2O3上以空气为氧化剂的丁二烯气相环氧化反应条件对催化剂性能的影响.宏观动力学实验结果表明,依据Langmuir-Hinselwood机理推测的动力学表达式与实验结果吻合较好,幂函数型的动力学表达式给出了在低丁二烯分压下,丁二烯的反应级数为1.9,O2的反应级数为1.1.丁二烯转化、生成乙烯基环氧乙烷及生成CO2的表观活化能分别为55.4 kJ/mol、 54.8 kJ/mol和64.6 kJ/mol.     

在Fe-Zn-Mg-Cr尖晶石结构催化剂上丁烯-2氧化动力学

用玻璃外循环无梯度反应器研究了在Fe-Zn-Mg-Cr尖晶石结构催化剂上丁烯-2氧化脱氢动力学。丁烯-2氧化脱氢动力学服从三步骤Redox机理。用脉冲法研究了催化剂用丁烯-2还原及还原催化剂用氧再氧化步骤。用脉冲法测定了丁烯-2吸附热。丁烯-2及丁二烯深度氧化动力学服从经验速度方程。用正交设计法估计了动力学方程的参数。丁烯-2氧化脱氢速度比丁烯-1要快。     

多组分氧化物Ag－Bi－V－Mo－O催化作用的光电子能谱研究

对于烃类选择氧化反应中复合氧化物的催化作用,普遍认为是Redox机理.迄今对于含有钥、秘复合氧化物催化剂的活性中心和作用机理还存在不同的看法.     

Redox机理动力学内扩散影响的特征

在Pb_0.88Bi_0.06La_0.02Mo/SiO₂催化剂上,反应在动力学区域进行时,甲醇氧化制甲醛服从Redox机理动力学方程:r=(k₁k₂P甲醇Po₂)/(0.5k₁P甲醇+k₂Po₂)当催化剂颗粒增大至3mm时,内扩散影响严重,催化剂有效因子在0.38-0.73之间,其内扩散区域的速度方程为r内=(Do₂/RTKL)2φ_M[K(Po₂-Po_2.o)-ln(1+Kpo₂/1+Kpo_2.o)]^1/2测定了反应受O₂内扩散控制时的反应活化能E内为74.5kJ/mol。     

在HZSM-5分子筛上甲醇脱水反应动力学研究——在活塞流反应器及连续搅拌槽式反应器中稳态反应的分析

以连续流动稳态法研究了甲醇在HZSM-5分子筛上生成二甲醚的反应动力学。使用活塞流反应器及连续搅拌槽式反应器,在150～190℃内分别得到相应的动力学数据。依据分子态吸附的甲醇在表面反应的可逆性及二甲醚吸附能力极弱的特性建立了反应机理模型,认为吸附态的与气相中的甲醇进行分子间反应生成二甲醚是速控步骤的Rideal-Eley机理。     

四丁基二锡氧烷催化合成碳酸二酯类化合物的新方法

 以四丁基二锡氧烷为催化剂，通过尿素的醇解反应，合成了四种\r\n高沸点碳酸二酯化合物．研究结果表明，尿素的第一步醇解反应较易进\r\n行，产物收率大于60％；第二步从氨基甲酸酯醇解变为碳酸二酯的反应\r\n较难进行．尿素醇解反应与所用的醇有密切的关系，其中尿素与苯甲醇\r\n醇解为碳酸二酯的反应最易进行，正己醇次之，而正辛醇反应最难进行\r\n．提高反应温度到195℃，以官能团为NCS的四丁基二锡氧烷代替官能团\r\n为Cl的四丁基二锡氧烷为催化剂时，适当提高醇的配比，尿素与正辛醇\r\n醇解为碳酸二酯的产物收率有较大的提高．提出了尿素醇解反应的可能\r\n机理．     

在HZSM—5分子筛上甲醇脱水反庆动力学研究：—在活塞流反应器及连续搅拌槽式反应器中稳态反应的分析

以连续动稳态法研究了甲醇在HZSM0－5分子筛上生成二甲醚的反应动力学，使用活塞流反应器及连续搅拌槽式反应器，在150－150℃内分别得到相应的动力学数据。依据分子态吸附的甲醇在表面反应的可逆性及二甲醚吸附能力极弱的特性建立了反应机理模型，认为吸附态的与气相中的甲醇进行分子间反应生成二甲醚是速控步骤的Rideal-Eley机理。     

非等温法研究TGDDM/DDS体系固化反应动力学

采用DSC对4,4′-四缩水甘油基二氨基二苯基甲烷(TGDDM)和3,3′-二氨基二苯基砜(DDS)体系的固化反应动力学进行了研究.分别通过n级反应法和Malek的最大概然机理函数法确定了固化反应机理函数,求解了固化反应动力学参数,得到了固化反应动力学模型.结果表明,通过Kissinger,Crane方法求解动力学参数所得到的n级反应模型与实验值差别较大;而采用Malek方法判别机理,表明该固化反应按照自催化反应机理进行,实验得到的DSC曲线与模型计算所得到的曲线吻合的较好,所确立的模型在5~20K/min的升温速率下能较好地描述TGDDM/DDS体系的固化反应过程,并为工艺参数的选择和工艺窗口的优化提供了理论依据.     

Transient absorption studies and numerical modeling of iodine photoreduction by nanocrystalline TiO2 films

We have used transient absorption spectroscopy to study the reaction between photogenerated electrons in a dye-free nanocrystalline titanium dioxide film and an iodine/iodide redox couple. Recombination kinetics was measured by recording the transient optical signal following band gap excitation by a UV laser pulse. In the presence of a methanol hole scavenger in the electrolyte, a long-lived (0.1-1 s) red/infrared absorbance is observed and assigned to photogenerated electrons forming Ti(3+) species. In the presence of iodine and excess iodide in the electrolyte, the signal decays on a millisecond-microsecond time scale, assigned to reduction of the redox couple by photogenerated electrons in the TiO(2). The electron lifetime decreases inversely with increasing iodine concentration, indicating that the back reaction is first order in [I(2)]. No evidence for I(2)(-) is observed, indicating that the reaction mechanism does not involve the formation of I(2)(-) as an intermediate. The shape of the kinetics evolves from monoexponential at low [I(2)] to stretched-exponential as [I(2)] increases. A Monte Carlo continuous-time random walk model is implemented to simulate the kinetics and its [I(2)] dependence and used to address the order of the recombination reaction with respect to electron density, n. The model incorporates the diffusion of oxidized species from the electrolyte toward the TiO(2) surface as well as electron trapping and transport in the TiO(2). In the limit of low [I(2)], the monoexponential kinetics is explained by the recombination reaction being rate limited by the diffusion of the oxidized species in the electrolyte. The stretched-exponential behavior at high [I(2)] can be explained by the reaction being rate limited by the transport of electrons through a distribution of trap states toward reactive sites at the TiO(2)-electrolyte interface, similar to the mechanism proposed previously for the kinetics of electron-dye cation recombination. Such trap-limited recombination can also explain the superlinear dependence of electron recombination rate on electron density, which has been reported elsewhere, without the need for a reaction mechanism that is second order in n. In contrast, a second-order reaction mechanism in a trap-free medium cannot explain the observed kinetics, although a second-order mechanism incorporating electron trapping cannot be conclusively ruled out by the data. We propose that the most likely reaction scheme, that is first order in both [I(2)] and n, is the dissociative reduction of I(2) onto the metal oxide surface, followed by a second electron reduction of the resulting adsorbed iodine radical, and that empirical second-order behavior of the electron lifetime is most likely explained by electron trapping rather than by a second-order recombination mechanism.     

Catalytic effect of copper on the hexacyanoferrate(III)-cyanide redox reaction-I The uncatalysed and catalysed reactions

A kinetic study of the hexacyanoferrate(III)-cyanide redox reaction has been made in connection with development of a new catalytic method for copper. The reaction kinetics change with time from first- to second-order dependence with respect to hexacyanoferrate(III). The reaction is nearly inverse first-order with respect to hexacyanoferrate(II) and first-order with respect to cyanide. The reaction shows a strong positive primary salt effect, but a very small increase in the reaction rate with temperature is found. A parallel reaction proceeds with a first-order dependence with respect to hydroxide. A tentative mechanism is proposed for the first reaction, involving the formation of cyanogen radicals. The second reaction corresponds to the well-known decomposition of hexacyanoferrate(III) in alkaline medium. The catalysed reaction exhibits similar kinetics with respect to hexacyanoferrate(II) and (III) but is zero-order with respect to cyanide and hydroxide and first-order with respect to catalyst. The proposed mechanism involves two consecutive interactions of the hexacyanoferrate(III) with copper(I) and with copper(II) cyanide complexes respectively, followed by a 2-electron oxidation of a co-ordinatively bridging cyanide group.     

Oxidation of benzaldehyde in films by Oxo-Cr(V) salen derivatives at solid/liquid interface

The oxidation of benzaldehyde as a film on a solid surface by various substituted oxochromium(V) salen in solution has been studied by monitoring the change in contact angle of the oxidant at the film/liquid interface utilizing a Teflon cell of known hydrodynamics and controlled convection/diffusion. The kinetics of the redox reaction in bulk has been monitored by measuring the change in absorbance of the oxidant solution. The interfacial study permits analysis of adsorption of the oxidant followed by the oxidation of the substrate under pseudo-first-order conditions. A comparison of the independent surface-averaged kinetic data with those obtained in the solution phase oxidation reaction is made and a model is presented for the mechanism of the interfacial reaction. The kinetic investigation shows that the rate of oxidation is accelerated in the presence of an electron-withdrawing group and is faster at the solid/liquid interface compared to the bulk. The probable mechanism of the redox reaction is discussed.     

KINETIC STUDY OF CARBONYLATION OF METHANOL TO ACETIC ACID AND ACETIC ANHYDRIDE OVER A NOVEL COPOLYMER-BOUND CIS-DICARBONYLRHODIUM COMPLEX

The kinetic study of carbonylation of methanol-acetic acid mixture to acetic acid and acetic anhydride over a cis-dicarbonylrhodium complex (MVM' Rh) coordinated with the ethylene diacrylate (M') crosslinked copolymer of methyl acrylate (M) and 2-vinylpyddine (V)shows that the rate of reaction is zero order with respect to both reactants methanol and carbon monoxide, but first order in the concentrations of promoter methyl iodide and rhodium in the complex. Polar solvents can accelerate the reaction. Activation parameters were calculated from the experimental results, being comparable to that of the homogeneous system. A mechanism similar to that of soluble rhodium catalyst was proposed.     

甲烷在CaO—Li—CeO2催化剂上氧化偶联反应宏观动力学

本文报导在CaO-Li-CeO_2催化剂上甲烷氧化偶联反应的宏观动力学。在893-973K温度范围内测出了甲烷氧化偶联反应产物的生成速度及其对甲烷及氧分压的反应级数。根据这些数据计算出了甲烷转化和相应产物生成的表观活化能E。在此基础上对反应机理进行了初步探讨。     

Mechanism and Kinetics of Reactions of C1 Molecules on Cu-Based Catalysts

The mechanism and kinetics of reactions occurring in the course of natural gas processing into motor fuels and other chemical products are considered with emphasis on copper-based catalysts. The following reactions are considered: methanol and methyl formate syntheses, dimethyl ether synthesis from syngas and by methanol dehydration, water-gas shift reaction, steam reforming of methanol and its decomposition to produce syngas, and others. It is shown that a key role in the mechanisms of the above reactions belong to transformations of stable, strongly (irreversibly) chemisorbed species, and this fact determines the specific features of the schemes of their mechanisms and kinetic models. The use of the specific features of reaction mechanisms makes it possible to increase the process efficiency (methanol and dimethyl ether syntheses) and provide a high selectivity (methyl formate synthesis).     

TiO2薄膜光催化气相甲醇制氢

 在气相连续流动装置中以TiO2薄膜为光催化剂，对甲醇的脱氢反应进行了研究．考察了空速、光照时间和反应温度对甲醇转化率的影响以及产氢量与添加的水蒸气量和甲醇浓度的关系，并将TiO2薄膜催化剂的光催化活性与TiO2纳米粉体催化剂进行了比较．反应动力学研究表明，光催化甲醇脱氢反应为一级反应，其活化能为8．64kJ／mol．探讨了该反应的机理．     

甲醇制烯烃反应过程中SAPO-34催化剂积炭动力学研究

在固定床反应器中研究了甲醇制烯烃反应过程中SAPO-34分子筛催化剂的积炭动力学，分别得到了催化剂积炭量与反应温度、剂醇比的经验关联式。结果表明，催化剂床层存在明显的积炭分布，在450 ℃，甲醇WHSV为15 h－1，催化剂积炭量随催化剂反应运行时间（Time on Stream, TOS）为25 min时，床层入口处的积炭量平均为9.56%，而出口处的积炭量平均为3.20%，属于平行失活，积炭主要来源于甲醇生成的高碳中间体，这些中间体在生成低碳烃的同时生成积炭。从积炭的生成机理出发，得到了SAPO-34分子筛催化剂的积炭动力学机理模型，将催化剂积炭量与一定催化剂停留时间内反应过程中甲醇的转化量相关联，该模型形式同样简单，能够较好地拟合实验数据。     

甲醇直接气相羰基化反应动力学

甲醇直接气相羰基化研究 ,是在无任何促进剂下 ,ＣＯ与甲醇直接进行羰基化反应 ,这与目前公认的甲醇必须有碘化物作用下构成催化循环的间接羰化不同 ,在催化理论上有可能提出新的羰基化机理。彭峰等在甲醇直接气相羰基化方面 ,对具有高活性与选择性的非铑非卤素Ｍｏ Ｃ催化剂体系进行了系列研究 ,并取得了较好的实验结果[1～ 5] 。有碘甲烷参与的甲醇羰基化液相或者气相反应 ,大多数文献认为控制步骤是碘化物中Ｃ -Ｉ键的解离及ＣＯ的插入 ,羰基化反应是由一系列平行和连串反应组成的[6～ 8] 。催化剂类型不同得到的动力学参数也不相同 ,难…