K2O助剂对合成碳酸二甲酯用Cu/Ni/ZrO2-SiO2催化剂的吸附和催化性能的影响

 用等体积浸渍法制备了ZrO2－SiO2（ZrSiO）表面复合氧化物负载的Cu－Ni催化剂,并用IR,TPR,TPD及微反技术考察了K2O助剂对CO2和CH3OH在Cu－Ni／ZrSiO催化剂表面上的吸附及合成碳酸二甲酯（DMC）反应性能的影响．结果表明：加入K2O助剂使CO2在催化剂表面上的吸附增强,当n（K）／n（Cu＋Ni）＝15％时,CO2在催化剂表面上吸附后生成K2CO3;CH3OH在催化剂表面上的解离吸附态（CH3O－和H＋）的吸附减弱;CO2和CH3OH在Cu－Ni／ZrSiO催化剂表面上反应的主要产物为DMC,H2O,CO和CH2O;随着K2O助剂的加入,反应转化率及DMC选择性提高,副产物（CO和CH2O）的选择性下降．根据实验结果,探讨了K2O对催化剂表面活性中心电荷分布的影响．     

Kinetic study of transesterification of methyl acetate with n‐butanol catalyzed by NKC‐9

The transesterification of methyl acetate and n‐butanol catalyzed by cation‐exchange resin, NKC‐9, was studied in this work to obtain the reaction kinetics. The experiments were carried out in a stirred batch reactor at different temperatures (328.15, 333.15, 338.15, 343.15, 345.15 K) under atmospheric pressure. The effects of temperature, molar ratio of reactants, and catalyst loading on the reaction rate were researched under the condition of eliminating the effect of diffusion. The experimental data were correlated with a kinetic model based on the pseudo‐homogeneous catalysis. The kinetic equation describing the reaction catalyzed by NKC‐9 was developed. © 2008 Wiley Periodicals, Inc. Int J Chem Kinet 41: 101–106, 2009     

K_2O助剂对合成碳酸二甲酯用Cu-Ni/MoO_3-SiO_2催化剂吸附和反应性能的影响

用等体积浸渍法制备了MoO3 SiO2 (MoSiO)表面复合氧化物负载的Cu Ni K2 O催化剂。利用IR ,TPR ,TPD以及微反技术研究了K2 O助剂对CO2 和CH3OH在Cu Ni MoSiO催化剂表面上吸附和合成DMC(碳酸二甲酯 )反应性能的影响。结果表明 :K2 O助剂的加入 ,使CO2 在催化剂表面吸附强度增加 ,当K2 O含量达Cu Ni总量的 15 %时 ,CO2 在催化剂表面上吸附后生成K2 CO3;CH3OH在催化剂表面上的解离吸附态 (CH3O- H )的吸附强度减弱 ;CO2 和CH3OH在Cu Ni K2 O MoSiO催化剂表面反应主要产物为DMC ,H2 O ,CO和CH2 O。随着K2 O助剂的加入 ,反应转化率在 10 %之前增加 ,之后下降 ,DMC选择性稍有提高。副产物 (CO和CH2 O)的选择性下降。根据实验结果探讨了K2 O对催化剂表面活性中心的电荷分布的影响。     

K2O对合成DMC用Cu-Ni/V2O5-SiO2催化剂性能的影响

V2O5 SiO2(VSiO) supported Cu Ni K2O catalysts for the synthesis of dimethyl carbonate were prepared using isovolumic impregnation. Based on TPR,TPD, IR and micro reactor techniques, the effect of K2O on the adsorption and reaction of CO2 and CH3OH on the catalyst were characterized. The results show that addition of K2O exerts obvious influence on the charge distribution of the active sites on Cu Ni/VSiO catalyst,increases the intensities of CO2 horizontal adsorption state, while that of the dissociation state of methanol descends. When the ratio of K is above 15 ％, K2CO3 is formed on the catalyst. Moreover,the main reaction products of CO2 and CH3OH on Cu Ni K2O/VSiO catalyst are still DMC, H2O, CO and CH2O,and with the addition of K2O, the conversion of reactants rise, but the selectivity of by-products decreases.     

K_2O对合成DMC用Cu- Ni/V_2O_5- SiO_2催化剂性能的影响

K_2O是多种固体催化剂的有效助剂 .大多数金属表面对 CO_2的吸附非常弱,在过渡金属中加入碱金属助剂可以促进 CO_2的吸附活化 [1, 2].近期对这方面的研究主要集中在 Pt[3]、 Cu[4]、 Ru[5]和 Fe[6]等单晶金属面上 .我们已报导过 Cu- Ni/V2O5- SiO_2(VSiO)催化剂表面 CO_2和 CH_3OH吸附及其反应性能 [7, 8].本研究将 K_2O助剂引入到 Cu- Ni/VSiO催化剂中,进一步考察了 K_2O助剂对 CO_2和 CH_3OH吸附和反应性能的影响 .1实验部分 　　采用 Cu、 Ni氨络合物混合硝酸盐水溶液 (含 KNO3, K占 Cu、 Ni总原子数 5～ 15…     

Equilibres liquide-vapeur isothermes de melanges binaires de la piperidine et de la N-methyl piperidine avec certains ethers

The authors have measured the vapour pressure of the binary four systems, piperidin +1,4-dioxan, piperidin+tetrahydropyran, piperidin+tert-butyl methyl ether and N-methyl piperidin+tert-butyl methyl ether. The measurements were carried out using an isoteniscope built by J. Jose [1]. The vapour pressure, excess Gibbs free energies at 298.15 K, 303.15 K, 313.15 K, 323.15 K, 333.15 K and 343.15 K, are reported for these mixtures. The excess Gibbs free energies have been fitted to the Redlich-Kister equation.     

Enhancing the rate of the Diels-Alder reaction using CO2 + ethanol and CO2 + n-hexane mixed solvents of different phase regions

The reaction rate of the Diels-Alder reaction between N-ethylmaleimide and 9-hydroxymethylanthrance in CO2 + ethanol and CO2 + hexane mixed solvents of different compositions were determined by in situ UV/vis spectroscopy at 318.15 K and different pressures. The density of the mixed solvents at different pressures was also determined and the isothermal compressibility was calculated using the density data. The activation volume of the reaction was calculated based on the dependence of rate constant (kc) on pressure. It was demonstrated that the kc was very sensitive to the pressure in the mixed solvents near the critical region and the kc increased dramatically as pressure approached dew points, critical point, and bubble points of the mixed solvents. However, the kc in the mixed solvents outside the critical region or in pure CO2 was not sensitive to pressure. At suitable conditions, kc could be 40 times larger than that in acetonitrile. The activation volume of the reaction was nearly independent of pressure as the pressure was much higher than the phase separation pressure of the mixed solvents, while it increased considerably as pressure approached the bubble points, critical point, and dew points from high pressure. The clustering of the solvent molecules with the reactants and the activated complex in the reaction systems near the phase boundary in the critical region may be the main reason for the interesting phenomena observed. This work also shows that, using pure CO2 as the solvent, the reaction cannot be carried out in the critical region of the solvent due to the limitations of the reactants, while it can be conducted in the critical region of mixed solvents of suitable compositions, where the solvents are highly compressible and the reaction rate can be tuned effectively by pressure.     

Equilibres liquide-vapeur isothermes de melanges binaires formes de composes heterocycliques tels que: Morpholine,tetrahydropyranne, piperidine et 1,4-dioxane

The authors have measured the vapour pressure of four binary systems, morpholine+piperidine, morpholine+1,4-dioxane, morpholine+tetrahydropyrane and 1,4-dioxane+tetrahydropyrane. The measurements were carried out using an isoteniscope built by J. Jose [1]. The vapour pressure, excess Gibbs free energies at 298.15, 303.15, 313.15, 323.15, 333.15 and 343.15 K are reported for these mixtures. The excess Gibbs free energies have been fitted to the Redlich-Kister equation.     

Study on the phase behaviors,viscosities, and thermodynamic properties of CO2/[C(4)mim][PF(6)]/methanol system at elevated pressures

An apparatus to determine the vapor-liquid equilibria of CO(2)/ionic liquid (IL)/organic solvent multisystems and the viscosity of the liquid phase at elevated pressures has been constructed. The solubility of CO(2) in 3-butyl-1-methyl-imidazolium hexafluorophosphate ([C(4)mim][PF(6)]) and the viscosity of CO(2)-saturated [C(4)mim][PF(6)] have been studied at 313.15, 323.15, and 333.15 K and at pressures up to 12.5 MPa. The phase behavior of CO(2)/[C(4)mim][PF(6)]/methanol ternary mixture and the viscosity of the liquid phases at equilibrium condition have also been determined at 313.15 K and at 7.15 and 10.00 MPa. The partition coefficients of the components in the ternary system are calculated. Peng-Robinson equation of state and some thermodynamic functions are combined to calculate the fugacity coefficients of the components in the system. It demonstrates that the viscosity of the IL-rich phase decreases significantly with increasing pressure of CO(2), and the effect of temperature on the viscosity of CO(2)/IL mixture is not noticeable at high pressure, although the viscosity of the CO(2)-free IL decreases dramatically with increasing temperature. Compressed CO(2) may become an attractive reagent for reducing the viscosity of ILs in many applications. The mole fraction of methanol in the CO(2)-rich phase is much lower than that in the IL-rich phase; this indicates that the interaction between the IL and methanol is stronger than that between CO(2) and methanol. The fugacity coefficient of CO(2) in IL-rich phase is larger than unity, while that of methanol is much small than unity, which further suggests that methanol-IL interaction is much stronger than CO(2)-IL interaction. However, the CO(2)-IL interaction is stronger than the CO(2)-methanol interaction.     

超临界二氧化碳二元体系相平衡性质的研究

采用固定体积可视观察法测定了CO₂+甲苯、CO₂+环己烷、CO₂+正丁醛、CO₂+异丁醛、CO₂+甲醇及CO₂+乙醇二元体系的临界点性质,为超临界萃取和化学反应提供基础数据.在对二元体系相行为与单组分超临界相行为进行比较的基础上,对不同化学物质及不同配比的二元体系临界点与二氧化碳临界点之间的关系进行了讨论.     

CO2／H2和（CO／CO2）＋H2低压合成甲醇催化过程的本质

通过在Ｃｕ／ＺｎＯ／Ａｌ２Ｏ３催化剂上ＣＯ２＋Ｈ２，ＣＯ＋Ｈ２和（ＣＯ／ＣＯ２）＋Ｈ２催化反应动力学研究对合成甲醇动力学和反应机理进行了细致分析，提出合成甲醇的反应机理，解释了在（ＣＯ／ＣＯ２）＋Ｈ２合成甲醇过程中少量ＣＯ２的作用及合成甲醇的直接碳源。     

Thermodynamic and spectroscopic study of pentafluorobenzonitrile + N,N-dimethyl aniline and + isopropylcyclohexane

Excess enthalpies at 323.15 and 343.15 K for pentafluorobenzonitrile (C₆F₅CN) + N,N-dimethyl aniline are reported. The association constant of the 1—1 complex formed by these molecules in solution in cyclohexane has been determined spectrophotometrically at six temperatures, and the enthalpy of complex formation evaluated from the temperature dependence of the equilibrium constant. Excess enthalpies for pentafluorobenzonitrile + isopropylcyclohexane (chosen as a model mixture for comparison with the above mixture) have also been measured at 323.15 and 343.15 K. The spectroscopic and calorimetric measurements are found to correlate well. Below 300 K, pentafluorobenzonitrile + isopropylcyclohexane shows partial miscibility; the mutual solubility curve is also presented.     

Study on Coupled Chemiluminescene Reaction of Ru(l,10-PhenanthroIine)32+-Methanol-Ce(Ⅳ)

It was reported that some hydroxyl/carbonyl carboxylic acids can enhance the chemiluminescence light emission intensity of Ru(phen)₃²⁺(Phen=1,10-phenanthroline) with Ce(Ⅳ). Further studies showed that methanol can also enhance the light emission intensity. In sulfuric acid medium, methanol was oxidized by eerie sulfate, the rate of oxidation depended directly on the concentration of cerium(Ⅳ) and methanol. The reaction rate changes inversely with sulfuric acid. The reaction occurs without the intermediate formation of a complex.     

Reaction parameters influence on the catalytic performance of copper-silica aerogel in the methanol steam reforming

Steam reforming of methanol was carried out on the copper-silica aerogel catalyst.The effects of reaction temperature,feed rate,water to methanol molar ratio and carrier gas flowrate on the H_2 production rate and CO selectivity were investigated.M ethanol conversion was increased considerably in the range of about 240-300,after which it increased at a slightly lower rate.The used feed flowrate,steam to methanol molar ratio and carrier gas flowwere 1.2-9.0 m L/h,1.2-5.0 and 20-80 m L/min,respectively.Reducing the feed flowrate increased the H_2 production rate.It was found that an increase in the water to methanol ratio and decreasing the carrier gas flowrate slightly increases the H2production rate.Increasing the water to methanol ratio causes the lowest temperature in which CO formation was observed to rise,so that for the ratio of 5.0 no CO formation was detected in temperatures lower than 375℃.In all conditions,by approaching the complete conversion,increasing the main product concentration,increasing the temperature and contact time,and decreasing the steam to methanol ratio,the CO selectivity was increased.These results suggested that CO was formed as a secondary product through reverse water-gas shift reaction and did not participate in the methanol steam reforming reaction mechanism.     

Equilibres liquide-vapeur isothermes de melanges binaires de la piperidine et de la N-methyl piperidine avec certains ethers

The authors have measured the vapour pressure of the four binary systems, piperidine +tert-butyl methyl ether, piperidine +1,4 dioxane, piperidine + tetrahydropyrane and N-methyl piperidine +tert-butyl methyl ether. The measurements were carried out using an isoteniscope built by J. Jose [1], The vapour pressure, excess Gibbs free energies at 298.15, 303.15, 313.15, 323.15, 333.15 and 343.15 K, are reported for these mixtures. The excess Gibbs free energies have been fitted to the Redlich-Kister equation.

     

Adaptation of Cu/ZnO/Al_2O_3 to Temperature Change in Methanol Synthesis from CO_2 Hydrogenation

The induction behavior in CO2 hydrogenation was studied by varying the reaction temperature to investigate the adaptation of the Cu/ZnO/Al2O3 catalyst to the temperature change. The results indicated that a used catalyst had a tendency to keep the last running state in new reaction conditions for MeOH formation, and that this tendency was related to the difference in Cu/Cun+ ratio caused by CO2 and CO produced at different reaction temperatures. However, the reverse water-gas shift reaction (RWGS) induced at four temperatures was completely different from that of methanol synthesis. It implied that the two so-called competitive reactions in CO2+H2, RWGS and methanol synthesis, have different active centers.     

Computational study of the reaction of chlorinated vinyl radical with molecular oxygen (C2Cl3 + O2)

Eight exothermic product channels of the reaction of chlorinated vinyl radical (C2Cl3) with molecular oxygen (O2) have been investigated using ab initio quantum chemistry methods. The energetics of the reaction pathways were calculated at the second-order Moller-Plesset Gaussian-3 level of theory (G3MP2) using the B3LYP/6-311G(d) optimized geometries. It has been shown that the C2Cl3 + O2 reaction takes place via a barrierless addition to form the chlorinated vinylperoxy radical complex, which can decompose or isomerize to various products via the complicated mechanisms. Two major reaction routes were revealed, i.e., the three-member-ring reaction mechanism leading to ClCO + CCl2O, CO + CCl3O, CO2 + CCl3, Cl + (ClCO)2, etc., and the OO bond cleavage mechanism leading to O(3P) + C2Cl3O. The other mechanisms are shown to be unimportant. The results are validated by the calculations using the restricted coupled cluster theory [RCCSD(T)] with the complete basis set extrapolation. Variational transition state theory was employed to calculate the individual and total rate coefficients as a function of temperature and pressure (helium). The theoretical rate coefficients are in good agreement with the available experimental data. It was found that the total rate coefficients show strong negative temperature dependence in the range 200-2000 K. At room temperature (297 K), the total rate coefficients are shown to be nearly pressure independent over a wide range of helium pressures (1-10(9) Torr). The deactivation of the initial adduct, C2Cl3O2, is only significant at pressures higher than 1000 Torr. The three-member-ring reaction mechanism is always predominant over the OO bond cleavage.     

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…     

HZSM-5型分子筛硅铝比对一步法合成二甲醚的影响

以Cu/Zn/Al(摩尔比为6∶3∶1)甲醇合成催化剂与HZSM-5型分子筛混合,制备了一步法二甲醚合成催化剂。通过改用三种不同Si/Al摩尔比（摩尔比为25、38和50）的HZSM-5型分子筛,考察了催化剂中脱水组分（HZSM-5分子筛）的酸性对二甲醚合成的影响。结果表明,随着催化剂Si/Al摩尔比的降低,分子筛的酸性增强,使得CO单程转化率提高。当催化剂Si/Al＝38时,CO对二甲醚的选择性最高,可达到68.13％,其次是催化剂Si/Al＝50,选择性最差的是Si/Al＝25的催化剂。在553 K、 3 MPa和4 000 h－1的条件下,Si/Al＝25和Si/Al＝38的催化剂CO单程转化率和DME的选择性接近一致。在此条件下,两者的时空产率达到试验的最大值,分别为0.38 gDME/(gcat·h)和0.36 gDME/(gcat·h),在试验范围内,一步法合成二甲醚催化剂最佳的Si/Al摩尔比为25。