氧化锌催化二苯甲烷二氨基甲酸甲酯分解反应

 对氧化锌催化二苯甲烷二氨基甲酸甲酯(MDC)分解制二苯甲烷二异氰酸酯(MDI)反应进行了研究,考察了反应温度、反应时间、催化剂用量以及原料浓度等对反应的影响. 结果表明,适宜的反应条件为催化剂用量2.1%, MDC浓度3.5%, 反应温度260 ℃, 反应时间20～30 min, 此时MDC转化率为99.5%, MDI产率为40.0%, 碳化二亚胺改性二苯甲烷二异氰酸酯(C-MDI)的产率为49.7%. 进一步研究发现,15%的醋酸锌溶液经草酸铵沉淀(不陈化)后,在500 ℃下焙烧4 h得到六方相的氧化锌,晶体的平均粒径为100～200 nm, 以其为催化剂时MDC转化率为99.1%, MDI的产率为52.1%, 同时还得到27.7%的 C-MDI.     

4,4''''-二苯甲烷二胺与碳酸二甲酯合成4,4''''-二苯甲烷二氨基甲酸甲酯反应过程分析

对碳酸二甲酯(DMC)与4,4'-二苯甲烷二胺(MDA)合成4,4'-二苯甲烷二氨基甲酸甲酯(MDC)的反应过程进行了研究,采用质谱、元素分析、红外光谱以及核磁共振氢谱等手段,对反应中间产物和最终产物进行了分离、组成结构分析和确认.研究结果表明,该反应是一个经过中间产物的串联反应,主产物为MDC,中间产物结构为4-(4'-氨苯基)苯甲烷氨基甲酸甲酯.     

4,4′-二苯甲烷二胺与碳酸二甲酯合成4,4′-二苯甲烷二氨基甲酸甲酯反应过程分析

对碳酸二甲酯(DMC)与4,4′-二苯甲烷二胺(MDA)合成4,4′-二苯甲烷二氨基甲酸甲酯(MDC)的反应过程进行了研究,采用质谱、元素分析、红外光谱以及核磁共振氢谱等手段,对反应中间产物和最终产物进行了分离、组成结构分析和确认。研究结果表明,该反应是一个经过中间产物的串联反应,主产物为MDC,中间产物结构为4-(4′-氨苯基)苯甲烷氨基甲酸甲酯。     

4,4'-二苯甲烷二异氰酸酯的高效液相色谱分析

用甲醇做衍牛试剂,把4,4'-二苯甲烷二异氰酸酯(MDI)衍生成4,4'-二苯甲烷二氨基甲酸甲酯(MDC),通过高效液相色谱分析MDC的含量来计算MDI的含量.该方法可以将MDI与合成反应中其他化合物完全分离.在测定浓度范围内线性关系良好,方法简单快速,精密度与准确度高.方法既保护了MDI中活泼的异氰酸根,也不需使用运输和储存困难的MDI标准品,能很好地用于化学合成中该产物的分析.     

一步催化合成二苯甲烷二氨基甲酸甲酯

研究了以H4SiW12O40-ZrO2/SiO2为催化剂,碳酸二甲酯(DMC)、苯胺和甲醛溶液为原料,一步催化合成二苯甲烷二氨基甲酸甲酯(MDC)的反应,考察了反应时间、反应温度和H4SiW12O40负载量等反应条件对催化性能的影响.适宜的反应条件是:DMC/苯胺/甲醛摩尔比为20/1/0.05,H4SiW12O40负载量为10%,443 K下反应7 h后降温到373 K下反应4.5 h.在此优化条件下,MDC的收率为24.9%.     

纳米Cu2O催化二苯甲烷二氨基甲酸苯酯无溶剂热分解制备二苯甲烷二异氰酸酯

研究了无溶剂条件下纳米Cu₂O催化二苯甲烷二氨基甲酸苯酯(MDPC)热分解制备二苯甲烷二异氰酸酯(MDI),考察了纳米Cu₂O的制备条件与反应条件对MDPC热分解反应性能的影响.结果表明,水解法制备的纳米Cu₂O在Ar中于300℃焙烧2h,其催化性能最佳;最佳的反应条件为Cu₂O用量为原料总重的0.06%,反应温度220℃,反应压力0.6kPa,反应时间12min,此时MDPC转化率达到99.8%,MDI选择性86.2%.     

Sb2O3催化二苯甲烷二氨基甲酸苯酯无溶剂热分解制备二苯甲烷二异氰酸酯

研究了无溶剂条件下Sb2O3催化二苯甲烷二氨基甲酸苯酯(MDPC)热分解制备二苯甲烷二异氰酸酯(MDI),考察了Sb2O3的制备条件与反应条件对MDPC热分解反应性能的影响.结果表明,立方相Sb2O3于400℃焙烧3 h,催化性能最好;适宜的反应条件为立方相Sb2O3用量为原料总重的1.0%,于220℃、0.67 kPa,反应12 min,此时MDPC转化率达到99.3%,MDI选择性84.4%.     

Co-MCM-41催化氧化二苯甲烷制备二苯甲酮的反应条件

系统地研究了Co掺杂MCM-41用于液相催化氧化二苯甲烷的反应,并探讨了不同溶剂及溶剂用量、反应时间、反应温度、催化剂用量等对二苯甲烷氧化反应的影响;并得出较优的反应条件:m(二苯甲烷)∶m(催化剂)=10∶1;V(二苯甲烷)∶V(冰醋酸)=1∶10;温度为100℃,时间为10 h,二苯甲烷的转化率21%,二苯甲酮的选择性95.8%。     

铅化合物催化二氨基二苯甲烷与碳酸二甲酯反应机理的红外光谱研究

研究了Pb(OAc)₂·3H₂O催化二氨基二苯甲烷(MDA)与碳酸二甲酯(DMC)反应合成二苯甲烷二氨基甲酸甲酯(MDC)的稳定性和成分变化, 发现乙酸铅在反应过程中会形成含氨基配体的碱式碳酸铅, 该化合物对MDC的合成仍具有较高活性. 采用红外光谱结合原位控温液体池技术研究了其催化机理, 结果表明, 铅催化剂的配体对其催化活性起重要作用, 双齿配位方式向单体配位方式的转变是催化剂起作用的关键步骤; 并在此基础上提出了铅催化剂催化MDA与DMC反应的机理.     

二苯甲烷二氨基甲酸酯的合成方法

综述了二苯甲烷二氨基甲酸酯的合成方法,讨论了合成二苯甲烷二氨基甲酸酯所涉及的甲基化试剂、催化剂。参考文献31篇。     

Synthesis and Thermal Behavior of 1,8-Dihydroxy- 4,5-dinitroanthraquinone Manganese Salt

A novel energetic combustion catalyst, 1,8-dihydroxy-4,5-dinitroanthraquinone manganese salt （DHDNEMn）, was synthesized by virtue of the metathesis reaction in a yield of 91%, and its structure was characterized by IR, element analysis and differential scanning calorimetry（DSC）. The thermal decomposition reaction kinetics was studied by means of different heating rate DSC. The results show that the apparent activation energy and pre-exponential factor of the exothermic decomposition reaction of DHDNEMn obtained by Kissinger＇s method are 162.3 kJ/mol and 1011.8 s^-1, respectively. The kinetic equation of major exothermic decomposition reaction of DHDNEMn is dα/dT= 10^118/β 2/5（1-α）[-ln（1-α）[-ln（1-α）]^3/5 exp（-1.623×10^5/RT）. The entropy of activation（△S^≠）, enthalpy of activation（△H^≠） and free energy of activation（A△G^≠） of the first thermal decomposition are -24.49 J·mol^-1·K^-1, 185.20 kJ/mol and 199.29 kJ/mol（T=575.5 K）, respectively. The self-accelerating decomposition temperature（TSADT） and critical temperature of thermal explosion（Tb） are 562.9 and 580.0 K, respectively. The above-mentioned information on the thermal behavior is quite useful for analyzing and evaluating the stability and thermal safety of DHDNEMn.     

咪唑钴(III)配合物还原动力学机理研究

配合物间的电子转移反应是近代化学中重要的一类反应［‘，’J，对于大多数反应来说，由于前驱配合物离子对形成常数较小，难以独立分离出各基元步骤动力学参数问；给研究带来困难问．为了丰富电子转移反应研究内容，寻找更多可供详细研究的反应体系，在前文报导［Fe（CN）6p还原高位阻［Co（tmen）3p”的反应动力学研究基础上＊，本文进一步合成了含有生物体系中常见配体咪哩（IInll）的Co仰）配合物［Co（NH。）。（ImH）］（CIO小和t，an。－［Co（NH。）（en）。（IInH）］（C104）。，再以［Fe（CN）6p为还原剂，考察了两C…     

电子陶瓷粉BaTiO3的液相合成技术(Ⅲ)──前驱体草酸氧钛钡的热分解反应动力学研究

以Brodio线性化简单图解法对前驱体草酸氧钛钡热分解过程中三段动力学参数进行了计算。结果表明,三段热分解的反应级数分别为2、2和0,活化能为96.8、165.1和172.2kJ/mol,频率因子为1.03×10¹¹、5.64×10⁸和2.63×10⁶s^-1.由热分解动力学参数优化热处理工艺制得高纯超细BaTiO₃粉体。     

柠檬酸铋的热分解机理、 非等温反应动力学及其对双基推进剂燃烧的催化作用

用TG和DSC以及变温固相原位反应池/傅里叶红外光谱(RSFTIR)联用技术研究了柠檬酸铋的热分解行为, 提出了可能的反应机理, 并计算了主分解反应的动力学参数. 柠檬酸铋主分解反应的表观活化能和指前因子分别为213.82 kJ/mol和1016.48 s^-1. 将柠檬酸铋应用到双基推进剂配方中研究其对双基推进剂燃烧性能的影响, 结果表明, 柠檬酸铋对双基推进剂燃烧有良好的催化作用, 能显著提高双基推进剂的燃速, 降低压力指数, 特别是与少量炭黑(CB)复合后, 对双基推进剂燃烧的催化效果更好.     

Kinetics and Mechanism of Exothermic First-stage Decomposition Reaction of 2,6-Bis （2,2,2-trinitroethyl）glycoluril

The thermal behavior, mechanism and kinetic parameters of the exothermic first-stage decomposition of the title compound in a temperature-programmed mode were investigated by means of DSC, TG-DTG and IR. The reaction mechanism was proposed. The kinetic model function in differential form, apparent activation energy(Ea) and pre-exponential factor(A) of this reaction are (3/2)(1-a)[-ln(1-a)]1/3, 185.52 kJ/mol and 1017.78 s-1, respectively. The critical temperature of the thermal explosion of the compound is 201.30 ℃. The values of ΔS≠, ΔH≠ and ΔG≠ of this reaction are 72.46 J/(mol · K), 175.1 kJ/mol and 141.50 kJ/mol, respectively.     

Ni-Mg复合催化剂催化裂解CH_4制氢动力学研究

基于定温热重实验,建立了甲烷催化裂解反应动力学模型和催化剂表面积炭失活动力学模型。其中,甲烷催化裂解动力学模型将初始产氢速率视为催化剂未积炭条件下的动力学基础数据;催化剂表面积炭失活动力学则基于甲烷催化裂解速率的降低。实验使用Ni-Mg复合催化剂,分别在535、585、635℃,甲烷分压10~4、2×10~4、3×10~4Pa条件下展开甲烷催化裂解动力学特性研究。结果表明,甲烷催化裂解的反应级数为0.5,活化能为82 k J/mol;Ni-Mg复合催化剂反应失活级数为0.5,催化剂失活活化能为118 k J/mol。实验条件下均制得了多壁碳纳米管。     

聚甲基丙烯酸甲酯热氧化降解的化学动力学研究

使用质谱、热分析手段研究了PMMA热解反应.结果表明,在氮气中,PMMA-CH=CH2有两个失重阶段,分别对应于主链末端双键引发的断链和主链无规则断链反应,转折点的失重率约为26%.其中,第一阶段的失重速率受扩散过程控制,平均表观活化能E为158.5 kJ/mol, lnA为27.69;第二失重阶段为1.5级化学反应,平均表观活化能E为214.79 kJ/mol, lnA为40.46.在空气中, PMMA也有两个失重阶段,反应机理为1级化学反应,转折点处的失重率约为70%.其中在第一失重阶段平均表观活化能E为130.32 kJ/mol, lnA为24.81,在此阶段中, 过氧化基团的分解反应对PMMA的失重速率有重要影响; 在空气中第二失重阶段平均表观活化能E为 78.25 kJ/mol, lnA为13.97.     

An investigation of the lowest reaction pathway of propene + BCl3 decomposition in chemical vapor deposition process

The lowest reaction pathway or one of the favored possible paths in the CVD process of preparing boron carbides with BCl₃-C₃H₆(propene)-H₂ precursors was searched theoretically, which involves 95 transition states and 103 intermediates. The geometries of the species were optimized by employing the B3PW91/6-311G(d,p) method. The transition states as well as their linked intermediates were confirmed with frequency and the intrinsic reaction coordinates analyses. The energy barriers and the reaction energies were evaluated with the accurate model chemistry method at G3(MP2) level after a non-dynamical electronic correlation detection. The heat capacities and entropies were obtained with statistical thermodynamics, and the heat capacities were fitted into analytical equations. The Gibbs free energies at 298.15 K for all of the reaction steps were reported. The energies at any temperature could be derived classically by using the analytical heat capacities. All the possible elementary reactions, including both direct decomposition and the radical attacking dissociations, for each reaction step were examined, and the one with the lowest energy or energy barrier was further studied in the next step. It was found that there are 19 reaction steps in the lowest path to produce the final BC₃ cluster including two steps of initializing the reaction chain of producing H and Cl radicals. The highest energy in the lowest reaction pathway is 215.1 kJ/mol at 298.15 K and that for 1,200 K is 275.1 kJ/mol. The results are comparable with the most recent experimental observation of the apparent activation energy 208.7 kJ/mol.     

Determination of kinetic parameters and analytical pyrolysis of tobacco waste and sorghum bagasse

The thermal decomposition of tobacco waste and sorghum bagasse was investigated by non-isothermal thermogravimetric analyses, applying slow heating rates and well-defined conditions. The purpose of evaluating the decomposition was to estimate the kinetic parameters of the analyzed materials. Activation energies and Arrhenius exponential factors were inferred by different estimation methods: the classical methods of Ozawa and Starink and the independent parallel reactions model. The analytical pyrolysis was performed in a micro-pyrolyzer coupled to a gas chromatographer/mass spectrometer. Values of activation energy obtained with single step reaction models by the Ozawa method were: 103.94 kJ/mol for tobacco waste and 120.01 kJ/mol for sorghum bagasse, and by the Starink method - 135.95 kJ/mol for tobacco waste and 148.91 kJ/mol for sorghum bagasse. The independent parallel reaction model presented energy activation values of 39.7-272.0 kJ/mol for tobacco waste and 35.7-220.0 kJ/mol for sorghum bagasse. In analytical slow and fast pyrolysis of tobacco residue and sorghum bagasse, holocellulose and lignin-derived compounds were identified, as well as hydrocarbons and aromatic hydrocarbons. The kinetic behavior of the materials are presented and discussed. Our findings may be helpful in evaluating other types of lignocellulosic biomass.     

Reaction pathways of propene pyrolysis

The gas‐phase reaction pathways in preparing pyrolytic carbon with propene pyrolysis have been investigated in detail with a total number of 110 transition states and 50 intermediates. The structure of the species was determined with density functional theory at B3PW91/6‐311G(d,p) level. The transition states and their linked intermediates were confirmed with frequency and the intrinsic reaction coordinates analyses. The elementary reactions were explored in the pathways of both direct and the radical attacking decompositions. The energy barriers and the reaction energies were determined with accurate model chemistry method at G3(MP2) level after an examination of the nondynamic electronic correlations. The heat capacities and entropies were obtained with statistical thermodynamics. The Gibbs free energies at 298.15 K for all the reaction steps were reported. Those at any temperature can be developed with classical thermodynamics by using the fitted (as a function of temperature) heat capacities. It was found that the most favorable paths are mainly in the radical attacking chain reactions. The chain was proposed with 26 reaction steps including two steps of the initialization of the chain to produce H and CH₃ radicals. For a typical temperature (1200 K) adopted in the experiments, the highest energy barriers were found in the production of C₃ to be 203.4 and 193.7 kJ/mol. The highest energy barriers for the production of C₂ and C were found 174.1 and 181.4 kJ/mol, respectively. These results are comparable with the most recent experimental observation of the apparent activation energy 201.9 ± 0.6 or 137 ± 25 kJ/mol. © 2010 Wiley Periodicals, Inc. J Comput Chem, 2010