高温水中多产物反应模型的构建及机理研究

建立了高温水中的反应模型并采用密度泛函理论(DFT)对香叶醇在高温水中的反应路径进行了研究. 通过前线轨道分析确定了反应的可能性. 高温水中香叶醇的反应路径与常温水中不同, 从常态下的酸催化反应路径转变为高温水状态下的酸碱共催化路径, 计算所得反应能垒为205.8 kJ/mol. 分别计算分析了高温水环境和周围水分子对反应能垒的影响, 结果表明, 高温水对反应物零点能的影响最大为0.966 kJ/mol, 水分子个数的影响最大可达94.7 kJ/mol. 官能团周围水分子个数变化对反应所产生的的影响大于高温水环境的影响.     

氟化氢与乙烯加成反应的ab Initio分子轨道研究

用ab initio分子轨道理论研究和确定氟化氢对乙烯分子型加成反应的可能途径.考虑了两种可能的反应机制.一为经过一个四中心过渡态的顺式加成;另一为经过一垂直过渡态(氟化氢分子轴垂直于C=C双键并在其中点的上方).计算结果表明(STO-3G和4-31G),前者是可能的反应途径.计算的活化能是58.68kcal/mol(245.52kJ/mol),文献报道值是54±3kcal/mol(225.94±12.56kJ/mol).分析和讨论了反应过程中Mulliken集居数的变化.比较了过渡态附近该“给一受络合物”中电子得失情况的变化,并用前线轨道理论作了解释.根据反应过程中氟化氢的“非键对”参与情况,说明该顺式四中心加成途径不在Woodward-Hoffmann规则禁阻之列.     

H-ZSM-5分子筛上的乙烯二聚反应机理的理论计算研究

应用分子力学和量子力学联合的ONIOM2(B3LYP/6-31G(d,p):UFF)计算方法研究了H-ZSM-5分子筛上乙烯二聚反应的机理. 用40T簇模型模拟ZSM-5分子筛位于孔道交叉点的酸性位,对乙烯二聚过程的分步反应和协同反应两种机理进行了考察. 对于分步反应机理,乙烯分子首先通过π-氢键作用在酸性位形成稳定的吸附络合物,再进一步发生质子化并生成乙醇盐中间体,随后乙醇盐与第二个乙烯分子发生碳-碳键结合形成丁醇盐产物. 第一步质子化和第二步碳链聚合的活化能分别为152.88和119.45 kJ/mol, 表明乙烯质子化反应为速控步骤. 对于协同反应机理,乙烯质子化、碳-碳键和碳-氧键生成同时进行,生成丁醇盐,反应的活化能为162.30 kJ/mol, 略高于分步反应机理中的速控步骤. 计算结果表明这两种反应机理之间存在相互竞争.     

氮氧化物TEMPO清除过氧自由基的机理研究

采用密度泛函理论、微扰理论和前线分子轨道分析,对酸环境和无酸环境下的2,2,6,6-四甲基哌啶氮氧化物(TEMPO)捕获过氧自由基的机理进行了理论研究.研究结果表明,与B3LYP泛函相比,M06-2x泛函的计算结果更接近实验值,更适合于所研究的体系;在酸环境下,质子化的TEMPO经过质子耦合电子转移和电子转移两个反应过程清除过氧自由基,并获得再生;与之相比,在无酸条件下TEMPO清除过氧自由基的反应过程则较为复杂,包括了烷氧胺的生成、β-氢原子转移、碳中心自由基的解离和TEMPO的再生4个反应步骤.通过能量计算,酸性条件下反应活化能为35.6 kJ/mol,明显低于无酸环境下的96.8 kJ/mol,说明酸性条件更有利于TEMPO清除过氧自由基,并对这一现象的化学本质给予了理论解释.     

SBA-15分子筛羟基结构性质及其催化活性的理论研究

采用密度泛函方法对SBA-15分子筛簇模型化合物进行了计算模拟,重点研究了簇模型化合物羟基的几何构型和电子结构性质。从键级、前线分子轨道、静电势和质子化能等方面探讨了表面羟基的酸碱及氧化还原性质。分子筛模型化合物的静电势图显示SBA-15分子筛表面孤立羟基的H原子为分子筛表面的L酸性位,而氢键羟基的O原子则为分子筛表面的B碱性位。分子筛的前线分子轨道研究发现,表面羟基是分子筛表面的氧化还原活性位。计算得到的羟基SiO-H键级及形成的氢键键级分别在0.677 5～0.710 5和0.055 7～0.092 6范围,计算羟基OH的质子化能在1 471～1 589 kJ.mol-1范围。考察分子筛表面的质子化能显示未参与形成氢键的羟基H质子具有较强的B酸性。     

HCN消除反应机理的理论研究

采用密度泛函理论方法从HCN氧化和水解两个方面研究了HCN消除反应机理,并考虑了HCN的直接消除反应(途径Ⅰ和途径Ⅱ)和CuO上的HCN消除反应(途径Ⅲ和途径Ⅳ)。途径Ⅰ为HCN与2个O2分子生成CO2、NO和H原子;途径Ⅱ为HCN与1个O2分子和1个H2O分子生成 CO2和NH3;途径Ⅲ为CuO上HNCO水解为CO2和NH3;途径Ⅳ为CuO上HCN水解为CO和NH3。研究发现,途径III速控步骤的活化自由能垒为157.32 kJ/mol,比途径Ⅱ中HNCO水解降低12.34 kJ/mol;比途径Ⅳ降低了63.8 kJ/mol。可见,HNCO是HCN净化过程中的重要中间体,CuO的加入降低了反应能垒,促进了HCN消除。     

大气中一元酸催化亚硫酸分解反应的从头算及动力学研究

采用从头算的理论计算方法,在CCSD（T）/aug-cc-pVDZ//MP2/aug-cc-pVDZ水平下,对甲酸、乙酸、丙酸和硝酸催化亚硫酸分解成二氧化硫和水的微观反应机理进行了理论研究.结果表明,这4种一元酸均可使亚硫酸分解反应能垒显著降低,降低幅度由大到小的顺序为丙酸 > 乙酸 > 甲酸 > 硝酸.其中,丙酸甚至使反应能垒从裸反应时的99.84 kJ/mol降至27.24 kJ/mol.在此基础上,计算了200~320 K温度范围内4种一元酸催化亚硫酸分解反应的速率常数,并结合它们在大气中的实际浓度计算了有效速率常数.结果表明,在实际大气环境中,乙酸对亚硫酸分解反应的催化效果最为显著.当乙酸存在时,亚硫酸在室温下的大气寿命仅为0.02 s.     

HCNO分子裂解机理的理论研究

实验提示应用248 nm UV波长对HCNO分子进行直接光解, 该分子可能发生裂解, 得到某些产物. 为了揭示HCNO分子的裂解机理, 选择HCNO分子的一组相对能级作为理论研究的起始点, 即¹A' (0.00 kJ/mol), ³A' (255.01 kJ/mol), ³A" (282.37 kJ/mol)和¹A" (341.59 kJ/mol), 进而找到了合理的反应路径, 阐明了相应的裂解机理, 得到的主要产物为H＋NCO, HCN＋O和NH＋CO, 与实验提示的结果相符合.     

H-ZSM-5分子筛上环己烯芳构化反应历程的理论研究

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.     

羟基自由基引发的马来酸酐聚合反应机理AM1研究

用AM1方法计算了马来酸酐、羟基自由基及其加成产物α-羟基丁二酸酐基自由基的电子结构、电荷分布和键级.应用前线轨道理论和成键三原则研究了羟基自由基引发下马来酸酐聚合过程中α-羟基丁二酸酐基自由基活性中间体参与反应的可能性及其自由基聚合反应机理.计算结果表明:马来酸酐基态分子的HOMO和LUMO分别对应于双键CC的成键π-MO和反键π -MO;马来酸酐的羟基自由基加成反应活化能计算值为55 7kJ/mol;马来酸酐在羟基自由基引发下的自由基聚合产物是链式结构,与实验事实相符.     

Mechanistic information from low-temperature rapid-scan and NMR measurements on the protonation and subsequent reductive elimination reaction of a (diimine)platinum(II) dimethyl complex

A detailed kinetic study of the protonation and subsequent reductive elimination reaction of a (diimine)platinum(II) dimethyl complex was undertaken in dichloromethane over the temperature range of -90 to +10 degrees C by stopped-flow techniques. Time-resolved UV-vis monitoring of the reaction allowed the assessment of the effects of acid concentration, coordinating solvent (MeCN) concentration, temperature, and pressure. The second-order rate constant for the protonation step was determined to be 15200 +/- 400 M(-1) s(-1) at -78 degrees C, and the corresponding activation parameters are DeltaH = 15.2 +/- 0.6 kJ mol(-1) and DeltaS = -85 +/- 3 J mol(-1) K(-1), which are in agreement with the addition of a proton that results in the formation of the platinum(IV) hydrido complex. The kinetics of the second, methane-releasing reaction step do not show an acid dependence, and the MeCN concentration also does not significantly affect the reaction rate. The activation parameters for the second reaction step were found to be DeltaH = 75 +/- 1 kJ mol(-1), DeltaS = +38 +/- 5 J mol(-1) K(-1), and DeltaV = +18 +/- 1 cm(3) mol(-1), strongly suggesting a dissociative character of the rate-determining step for the reductive elimination reaction. The spectroscopic and kinetic observations were correlated with NMR data and assisted the elucidation of the underlying reaction mechanism.     

Mechanism of Gold(I)‐Catalyzed Conia‐ene Reaction of β‐Ketoesters with Alkynes: A DFT Study

Density functional calculations have been performed to comparatively investigate two possible pathways of Au(I)‐catalyzed Conia‐ene reaction of β‐ketoesters with alkynes. Our studies find that, under the assistance of trifluoromethanesulfonate (TfO), the β‐ketoester is the most likely to undergo Model II to isomerize into its enol form, in which TfO plays a proton transfer role through a 6‐membered ring transition state. The coordination of the Au(I) catalyst to the alkynes triple bond can enhance the eletrophilic capability and reaction activity of the alkynes moiety, which triggers the nucleophilic addition of the enol moiety on the alkynes moiety to give a vinyl‐Au intermediate. This cycloisomerizaion step is exothermal by 21.3 kJ/mol with an energy barrier of 56.0 kJ/mol. In the whole catalytic process, the protonation of vinyl‐Au is almost spontaneous, and the formation of enol is a rate‐limiting step. The generation of enol and the activation of Au(I) catalyst on the alkynes are the key reasons why the Conia‐ene reaction can occur in mild condition. These calculations support that Au(I)‐catalyzed Conia‐ene reactions of β‐ketoesters with alkynes go through the pathway 2 proposed by Toste.     

Elimination of methane from protonated acetaldehyde: The Ab initio transition state

The transition state (TS) for loss of CH₄ from protonated acetaldehyde has been located at the second-order Moller-Plesset (MP2)/6-31G(d,p) level of theory. The activation energy is predicted to be 263.9 kJ/mol starting from the more stable form (methyl and hydrogen E) and 261.6 kJ/mol starting from the less stable form (methyl and hydrogen Z) that is required for reaction. The products (methane and the formyl ion) are predicted to lie 136.6 kJ/mol below the TS for their formation. MP2 methods underestimate the heats of formation of both the TS and the reaction products by about 40 kJ/mol when compared with experiment. Restricted Hartree-Fock (RHF) calculations give much more accurate relative energies. The MP2 TS leads directly to fragmentation and is described as a protonation of the methyl group by the acidic proton on oxygen. Under RHF theory the reaction is stepwise. An RHF TS similar to the MP2 TS leads to a nonclassical intermediate (which is stable at this level of theory) that has one of the C---H bonds protonated. This mechanism (protonation of an alkyl group) appears to be a general one for high energy 1,2 eliminations from organic cations. (J Am Soc Mass Spectrom 1994, 5, 1102-1106)     

馏分油浆态床加氢处理研究: II FCC柴油加氢工艺条件及动力学研究

对FCC柴油在浆态床柴油加氢催化剂SP25上的加氢工艺条件进行了优化,并考察了加氢脱硫（HDS）和加氢脱氮（HDN）动力学。结果表明,提高反应温度、提高反应压力、增加催化剂的加入量、延长反应时间都能提高催化剂的加氢精制活性,最佳的FCC柴油浆态床加氢工艺条件为,温度350℃、压力6MPa、催化剂加入量6%、反应时间2h。催化剂循环使用性能的考察结果表明,SP25催化剂具有良好的活性稳定性。动力学研究结果表明,FCC柴油的加氢脱硫反应过程可以分为两个阶段。第一阶段为较易脱除的苯并噻吩类（BTs）硫化物的加氢脱硫反应,反应活化能为70.00kJ/mol;第二阶段为较难脱除的二苯并噻吩类（DBTs）硫化物的加氢脱硫反应,反应活化能为85.65kJ/mol。FCC柴油HDN反应的活化能为79.91kJ/mol。烷基取代的二苯并噻吩类硫化物（特别是DMDBTs）是加氢精制反应中最难脱除的含杂原子（S或N）烃类化合物。     

HTPB／TDI,HDI聚合反应动力学研究

对端羟基聚丁二烯／甲苯二异氰酸酯，端羟基聚丁二烯／己二异氰酸酯甲苯溶液体系进行了反应动力学研究，用基团分析方法计算了相应体系的活化能，并对无催化剂和有催化剂的体系作了比较。结果表明，二丁基二月桂酸象对上述体系有强的催化作用，使体系的活化能降低，反应速度加快。对于对端差基聚丁二烯／甲苯二异氰酸酯体系，无催化剂时前后期反应活化能分别为２９．１ｋＪ／ｍｏｌ、３７．４ｋＪ／ｍｏｌ，有催化剂时前后期反应活化     

Catalytic gasification of Pakistani Lakhra and Thar lignite chars in steam gasification

采用热重法在常压与700℃~900℃条件下的水蒸气气化过程,对两种巴基斯坦Lakhra和Thar褐煤半焦进行了单一和混合催化剂(即3%钙和5%钠-黑液单一催化剂及一种3%钙和5%钠-黑液混合催化剂)对碳转化率、气化反应速率常数及活化能、有害污染含硫气体相对量的催化效应研究.两者Lakhra和Thar褐煤半焦经直接气化就可获得高的碳转化率,但采用纸浆黑液催化剂可使气化速率变得很快.含灰高的Thar褐煤半焦在纸浆黑液催化气化过程更易生成一些复杂的硅酸盐,从而导致比含灰低的Lakhra褐煤半焦出现一个更低的转化率.在水蒸气气化过程由半焦和纸浆黑液自身所产生的SO2 和 H2S含硫气体可为存在于纸浆黑液中的Ca盐所捕获而完成脱硫过程,但这一过程在低于900℃时更有效.缩芯模型 (SCM)可较好地用来关联转化率与时间的关系并给出不同温度下的反应速率常数k.基于阿累尼乌斯方程预测了反应活化能Ea 和指前因子A.在纸浆黑液和钙混合催化及纸浆黑液催化剂时,Lakhra褐煤半焦的Ea分别为44.7kJ/mol和 59.6kJ/mol明显小于Thar褐煤半焦的Ea=114.6kJ/mol 和 Ea=100.8kJ/mol,同样也小于无催化剂纯半焦气化时Lakhra褐煤半焦的Ea=161.2kJ/mol和Thar半焦的Ea=124.8kJ/mol.     

Structure, reactivity and thermochemical properties of protonated lactic acid

The protonation energetics of lactic acid (LA) were experimentally determined by the kinetic method including the entropy effect. The values (proton affinity, PA(LA) = 817.4 +/- 4.3 kJ mol(-1); protonation entropy, DeltaS degrees (p)(LA) = -2 +/- 5 J K(-1) mol(-1); gas-phase basicity, GB(LA) = 784.5 +/- 4.5 kJ mol(-1)) agree satisfactorily with computed G2(MP2) expectations (PA(LA) = 811.8 kJ mol(-1); DeltaS degrees (p)(LA) = -7.1 J K(-1) mol(-1); GB(LA) = 777.4 kJ mol(-1)). The fragmentation behaviour of protonated lactic acid (LAH(+)) is dominated by carbon monoxide loss followed by elimination of a water molecule. Direct dehydration of LAH(+) is only a high-energy process hardly competitive with the CO loss. A complete mechanistic scheme, based on MP2/6-31G* calculations, is proposed; it involves isomerization of the various protonated forms of LA and the passage through the ion-neutral complex between the 2-hydroxypropyl acylium cation and a water molecule.     

A high yield method for the direct amidation of long-chain fatty acids

The amidation of long-chain fatty acids is the key step for preparing surfactants with excellent interfacial activity. Gas chromatography–mass spectrometry was employed to detect the reactants and products in the direct amidation reactions. The conversion and the concentration of the amides in the reaction process were also investigated to determine the best catalyst, the reaction rate constants, and activation energy. It was identified that the amidation reaction of the long-chain phenyl fatty acid was a zero-order reaction and 3,4,5-trifluorophenylboronic acid was the most effective catalyst by which the activation energy reduced to 55.79 kJ/mol from 95.44 kJ/mol. The method can be applied to other long-chain fatty acids, saturated or unsatureated. The turning-over-temperature was 156°C, over which high yields can be achieved without any catalyst. These provide a reference for the preparation of long-chain fatty acid amides.     

Methane activation and oxidation in sulfuric acid

The H/D exchange observed when methane is contacted with D(2)SO(4) at 270-330 degrees C shows that the alkane behaves as a sigma base and undergoes rapid and reversible protonation at this temperature. DFT studies of the hydrogen exchange between a monomer and a dimer of sulfuric acid and methane show that the transition states involved in the exchange are bifunctional, that is one hydrogen atom is transferred from a hydroxy group in sulfuric acid to methane, while one hydrogen atom is abstracted from methane by a non-hydroxy oxygen atom in sulfuric acid. All the transition states include a CH(5) moiety, which shows similarities to the methanium ion CH(5) (+). The calculated potential activation energy of the hydrogen exchange for the monomer is 174 kJ mol(-1), which is close to the experimental value (176 kJ mol(-1)). Solvation of the monomer and the transition state of the monomer with an extra sulfuric acid molecule, decrease the potential activation energy by 6 kJ mol(-1). The acid-base process is in competition, however, with an oxidative process involving methane and sulfuric acid which leads to CO(2), SO(2), and water, and thus to a decrease of acidity and loss of reactivity of the medium.     

CO_(2)加氢制甲酸理论研究及高效铁基催化剂设计北大核心CSCD

CO_(2)加氢制甲酸由于需同时活化惰性氢气及CO_(2)而富有挑战性,同时此过程原子经济性100%,具有很好的理论和现实研究价值,但文献中报道的活性较好的催化剂均为贵金属催化剂.为了开发活性更高的用于CO_(2)加氢制甲酸的铁基催化剂,我们采用理论计算方法研究了12种不同种类的PNP-Fe(PNP=2,6-(二-叔丁基-磷甲基)吡啶)化合物催化CO_(2)加氢制甲酸的过程.理论研究结果表明,CO_(2)加氢制甲酸反应过程包括H2活化及CO_(2)插入金属氢键两个步骤,H_(2)活化过程是整个反应的速控步骤.催化剂吡啶环上进行P原子取代可以显著降低H_(2)活化能垒.基于以上发现,我们设计了一种新颖的高效铁基催化剂,使用此催化剂催化CO_(2)加氢制甲酸反应,速控步骤能垒只有85.6 kJ/mol,催化活性与贵金属的比较接近.我们研究的12种铁基催化剂速控步骤能垒范围为85.6~126.4 kJ/mol,显示了配体良好的调控催化活性能力.