丙烯环氧化反应中失活钛硅分子筛的无氧脱附研究

采用无氧脱附方法对丙烯环氧化中失活的薄层钛硅分子筛(即Spent EPO-4)和环氧丙烷(PO)与丙二醇单甲醚(MME)浸渍的TS-1催化剂(即PO／TS-1和MME／TS-1)进行了研究，脱附产物由气相色谱定性分析，无氧脱附后的催化剂以丙烯环氧化为探针反应进行再生性能评价，同时在无氧条件下考察了TS-1在300℃时催化裂化PO反应．实验结果表明：PO浸渍TS-1可使其活性明显下降，PO在TS-1上不是简单的弱吸附，存在着化学强吸附和自聚．失活催化剂(Spent EPO-4和PO／TS-1)经无氧脱附后，其催化活性可显著恢复．通过对失活催化剂脱附产物的比较，推测了丙烯环氧化反应过程中钛硅分子筛失活原因．     

氢氧混合体系下Ag／TS－1催化剂上丙烯的高效环氧化反应

 在氢氧混合体系中，沉积-沉淀法制备的Ag/TS-1催化剂对丙烯环氧化反应具有高的催化活性和选择性。本文主要考察了载体TS-1的硅钛比和反应温度对催化剂性能的影响。结果表明：当载体TS-1硅钛比为64，反应温度150℃时，2wt%Ag/TS-1催化剂表现出优异的催化性能，丙烯转化率和环氧丙烷选择性可分别达1.37%和93.51%。     

TS-1催化丙烯环氧化过程中环氧丙烷的开环反应研究

环氧丙烷的开环反应是TS-1催化丙烯环氧化制备环氧丙烷过程的副反应,本文对醇溶剂中开环反应进行了研究,分析了该反应的酸性催化机理,酸性主要来自TS-1与H2O2的相互作用产生的质子酸,醇溶剂能显著增强体系酸性从而加快环氧丙烷的开环反应速度。三种醇按酸性增强程度的顺序为甲醇>异丙醇>仲丁醇。根据反应的Eley-Rideal 机理（吸附态的PO与游离态的醇发生开环反应,表面反应为控制步骤）再考虑各组分在TS-1上的吸附特点提出反应的机理模型。用实验数据进行了回归,得到了令人满意的动力学方程式,实验数据与模型计算值平均偏差小于10％。     

TS-1/尿素/过氧化氢体系中的丙烯环氧化反应

 研究了TS-1/尿素/过氧化氢体系中的丙烯环氧化反应,考察了尿素用量和过氧化氢浓度对反应的影响. 结果表明,加入适量尿素可以显著提高环氧丙烷选择性和过氧化氢的利用率,而提高过氧化氢浓度不利于丙烯环氧化反应. 在尿素用量为31.2 g/L和过氧化氢浓度为0.09 mol/L时,过氧化氢转化率可达90.00%,环氧丙烷选择性可达96.12%,过氧化氢利用率可达98.46%.     

添加吐温40合成钛硅分子筛TS-1

 以自制的四丙基氢氧化铵（TPAOH）水溶液为模板剂，采用在水热晶化合成体系中添加少量非离子表面活性剂——吐温40的方法,合成了钛硅分子筛TS-1，可以明显减少TPAOH的用量，而且在一天之内，即可得到纳米尺寸的TS-1。运用XRD、TEM、BET、FT-IR及UV-Vis等表征手段考察了TS-1的结构及物理性能，并以丙烯环氧化为探针反应，考察其催化性能，得到的结果表明，用这种方法合成的TS-1样品具有较高的结晶度和较大的比表面积，晶貌呈均匀的立方体状，颗粒尺寸在100 nm左右，并且样品中含有极少量锐钛矿型TiO2，其催化丙烯环氧化反应性能较好。     

分子氧为氧化剂的Au?Ag/TS-1光催化剂协同光催化丙烯气相环氧化

近年来,丙烯环氧化已引起人们广泛的兴趣;然而,大多数过程仍面临分离困难等问题.此外,丙烯转化率和环氧丙烷(PO)的选择性仍然非常低.从环境和经济观点来看,分子氧是丙烯选择性环氧化的理想氧化剂.开发一种气相光催化环氧化方法,即在光能和多相光催化剂存在的情况下,用于化学品生产.因此,本文探讨了通过光催化O2选择氧化丙烯环氧化.传统的制备方法存在环境污染及能耗大等缺点,而利用氧气直接进行光催化丙烯环氧化制备环氧丙烷是相当具有前景的化学品生产途径.本文采用水热法制备了微球状TS-1载体,再通过浸渍还原法制备了不同Au/Ag质量比的Au–Ag/TS-1双金属催化剂.通过X射线衍射、扫描电镜、紫外-可见吸收光谱、透射电镜、X射线光电能谱、荧光光谱和N2吸脱附法等手段对合成的催化剂的组成、形貌和性质进行了研究,通过气相色谱在线分析得到光催化反应结果.结果表明,通过浸渍还原法可以很好的将贵金属分散到载体表面上.对于Au–Ag/TS-1双金属催化剂,当Au/Ag质量比为4/1时,反应温度为443 K时,环氧丙烷生成速率最大(68.3μmol/(g·h)),其选择性达52.3%.对于Au–Ag/TS-1光催化剂,双金属负载有利于O2吸附活化,同时促进了电子的传递,从而抑制电子空穴的复合,有利于氧自由基的形成.结果表明,Au,Ag双金属之间存在协同催化作用,根据实验现象提出了一种可能的反应机理.     

分子氧为氧化剂的Au-Ag/TS-1光催化剂协同光催化丙烯气相环氧化（英文）

近年来,丙烯环氧化已引起人们广泛的兴趣;然而,大多数过程仍面临分离困难等问题.此外,丙烯转化率和环氧丙烷(PO)的选择性仍然非常低.从环境和经济观点来看,分子氧是丙烯选择性环氧化的理想氧化剂.开发一种气相光催化环氧化方法,即在光能和多相光催化剂存在的情况下,用于化学品生产.因此,本文探讨了通过光催化O_2选择氧化丙烯环氧化.传统的制备方法存在环境污染及能耗大等缺点,而利用氧气直接进行光催化丙烯环氧化制备环氧丙烷是相当具有前景的化学品生产途径.本文采用水热法制备了微球状TS-1载体,再通过浸渍还原法制备了不同Au/Ag质量比的Au.Ag/TS-1双金属催化剂.通过X射线衍射、扫描电镜、紫外-可见吸收光谱、透射电镜、X射线光电能谱、荧光光谱和N2吸脱附法等手段对合成的催化剂的组成、形貌和性质进行了研究,通过气相色谱在线分析得到光催化反应结果.结果表明,通过浸渍还原法可以很好的将贵金属分散到载体表面上.对于Au.Ag/TS-1双金属催化剂,当Au/Ag质量比为4/1时,反应温度为443 K时,环氧丙烷生成速率最大(68.3μmol/(g·h)),其选择性达52.3%.对于Au.Ag/TS-1光催化剂,双金属负载有利于O_2吸附活化,同时促进了电子的传递,从而抑制电子空穴的复合,有利于氧自由基的形成.结果表明,Au,Ag双金属之间存在协同催化作用,根据实验现象提出了一种可能的反应机理.     

丙烯在Au/TiO2催化剂上的化学吸附与临氢环氧化反应

环氧丙烷;丙烯环氧化;丙烯在Au/TiO2催化剂上的化学吸附与临氢环氧化反应     

钛硅分子筛催化1-丁烯环氧化反应溶剂效应和酸碱效应研究

研究了用双氧水为氧化剂，钛硅分子筛TS-1催化1-丁烯环氧化反应的溶剂效应．研究发现，在质子性溶剂中1-丁烯环氧化反应活性高于非质子性溶剂，而以甲醇为溶剂H2O2转化率最高．分别利用碱性添加物稀氨水溶液和酸性添加物稀盐酸溶液调变反应介质的pH值，考察了介质的pH值对1-丁烯环氧化反应的影响，结果表明，随pH值提高，1，2-环氧丁烷(B0)的选择性略提高，但是过量稀氨水的加入会导致催化剂失活，双氧水的转化率及利用率明显下降．与钛硅分子筛催化丙烯环氧化相比，酸性添加物的加入对反应结果的影响不大，随反应介质的pH值降低1，2-环氧丁烷的选择性没有明显下降．     

微波合成TS-1分子筛的催化性能研究

采用微波加热技术法合成TS-1分子筛, 以30%的H₂O₂水溶液为氧化剂, 考察了所合成的TS-1分子筛在苯乙烯和1-己烯环氧化反应中的催化性能, 并与传统水热法合成的TS-1进行了比较. 结果表明, 由微波合成TS-1的催化性能比传统水热法合成的TS-1更为优异. 采用XRD, FT-IR, UV-vis, SEM等手段对二者进行表征, 发现微波合成的TS-1晶粒与晶粒之间存在“粘连”现象, 这种现象降低了分子筛表面硅羟基含量, 增加了TS-1分子筛的疏水性, 使得分子筛对反应底物苯乙烯和1-己烯的吸附能力增强, 从而导致催化性能显著提高.     

Partial oxidation of propylene catalyzed by VO3 clusters: a density functional theory study

Density functional theory (DFT) calculations are carried out to investigate partial oxidation of propylene over neutral VO 3 clusters. C=C bond cleavage products CH 3CHO + VO 2CH 2 and HCHO + VO 2CHCH 3 can be formed overall barrierlessly from the reaction of propylene with VO 3 at room temperature. Formation of hydrogen transfer products H 2O + VO 2C 3H 4, CH 2=CHCHO + VO 2H 2, CH 3CH 2CHO + VO 2, and (CH 3) 2CO + VO 2 is subject to tiny (0.01 eV) or small (0.06 eV, 0.19 eV) overall free energy barriers, although their formation is thermodynamically more favorable than the formation of C=C bond cleavage products. These DFT results are in agreement with recent experimental observations. VO 3 regeneration processes at room temperature are also investigated through reaction of O 2 with the CC bond cleavage products VO 2CH 2 and VO 2CHCH 3. The following barrierless reaction channels are identified: VO 2CH 2 + O 2 --> VO 3 + CH 2O; VO 2CH 2 + O 2 --> VO 3C + H 2O, VO 3C + O 2 --> VO 3 + CO 2; VO 2CHCH 3 + O 2 --> VO 3 + CH 3CHO; and VO 2CHCH 3 + O 2 --> VO 3C + CH 3OH, VO 3C + O 2 --> VO 3 + CO 2. The kinetically most favorable reaction products are CH 3CHO, H 2O, and CO 2 in the gas phase model catalytic cycles. The results parallel similar behavior in the selective oxidation of propylene over condensed phase V 2O 5/SiO 2 catalysts.     

Potential energy surfaces, product distributions and thermal rate coefficients of the reaction of O(3P) with C2H4(X1Ag): a comprehensive theoretical study

The potential energy surface for the O((3)P) + C(2)H(4) reaction, which plays an important role in C(2)H(4)/O(2) flames and in hydrocarbon combustion in general, was theoretically reinvestigated using various quantum chemical methods, including G3, CBS-QB3, G2M(CC,MP2), and MRCI. The energy surfaces of both the lowest-lying triplet and singlet electronic states were constructed. The primary product distribution for the multiwell multichannel reaction was then determined by RRKM statistical rate theory and weak-collision master equation analysis using the exact stochastic simulation method. Intersystem crossing of the "hot" CH(2)CH(2)O triplet adduct to the singlet surface, shown to account for about half of the products, was estimated to proceed at a rate of approximately 1.5 x 10(11) s(-1). In addition, the thermal rate coefficients k(O + C(2)H(4)) in the T = 200-2000 K range were computed using multistate transition state theory and fitted by a modified Arrhenius expression as k(T) = 1.69 x 10(-16) x T(1.66) x exp(-331 K/T) . Our computed rates and product distributions agree well with the available experimental results. Product yields are found to show a monotonic dependence on temperature. The major products (with predicted yields at T = 300 K/2000 K) are: CH(3) + CHO (48/37%), H + CH(2)CHO (40/19%), and CH(2)(X(3)B(1)) + H(2)CO (5/29%), whereas H + CH(3)CO, H(2) + H(2)CCO, and CH(4) + CO are all minor (< or =5%).     

Theoretical study on the reaction mechanism of the methyl radical with nitrogen oxides

The radical-molecule reaction mechanism of CH3 with NOx (x = 1, 2) has been explored theoretically at the B3LYP/6-311Gd,p and MC-QCISD (single-point) levels of theory. For the singlet potential energy surface (PES) of the CH3 + NO2 reaction, it is found that the carbon to middle nitrogen attack between CH3 and NO2 can form energy-rich adduct a (H3CNO2) with no barrier followed by isomerization to b1 (CH3ONO-trans), which can easily convert to b2 (CH3ONO-cis). Subsequently, starting from b (b1, b2), the most feasible pathway is the direct N-O bond cleavage of b (b1, b2) leading to P1 (CH3O + NO) or the 1,3-H-shift and N-O bond rupture of b1 to form P2 (CH2O + HNO), both of which may have comparable contribution to the reaction CH3 + NO2. Much less competitively, b2 can take a concerted H-shift and N-O bond cleavage to form product P3 (CH2O + HON). Because the intermediates and transition states involved in the above three channels are all lower than the reactants in energy, the CH3 + NO2 reaction is expected to be rapid, as is consistent with the experimental measurement in quality. For the singlet PES of the CH3 + NO reaction, the major product is found to be P1 (HCN + H2O), whereas the minor products are P2 (HNCO + H2) and P3 (HNC +H2O). The CH3 + NO reaction is predicted to be only of significance at high temperatures because the transition states involved in the most feasible pathways lie almost above the reactants. Compared with the singlet pathways, the triplet pathways may have less contributions to both reactions. The present study may be helpful for further experimental investigation of the title reactions.     

Quantum chemical and statistical rate study of the reaction of O(3P) with allene: O-addition and H-abstraction channels

The lowest-lying triplet and singlet potential energy surfaces for the O(3P) + CH2=C=CH2 reaction were theoretically characterized using the complete basis set model chemistry, CBS-QB3. The primary product distributions for the multistate multiwell reactions on the individual surfaces were then determined by RRKM statistical rate theory and weak-collision master equation analysis using the exact stochastic simulation method. The results predict that the electrophilic O-addition pathways on the central and terminal carbon atom are dominant up to combustion temperatures. Major predicted end-products for the addition routes include CO + C2H4, 3CH2 + H2CCO, and CH2=C*-CHO + H*, in agreement with experimental evidence. CO + C2H4 are mainly generated from the lowest-lying singlet surface after an intersystem crossing process from the initial triplet surface. Efficient H-abstraction pathways are newly identified and occur on two different electronic state surfaces, 3A' and 3A', resulting in OH + propargyl radicals; they are predicted to play an important role at higher temperatures in hydrocarbon combustion chemistry and flames, with estimated contributions of ca. 35% at 2000 K. The overall thermal rate coefficient k(O + C3H4) at 200-1000 K was computed using multistate transition state theory: k(T) = 1.60 x 10(-17) x T (2.05) x exp(-90 K/T) cm3 molecule(-1) s(-1), in good agreement with experimental data available for the 300-600 K range.     

A temperature-dependent relative-rate study of the OH initiated oxidation of n-butane: the kinetics of the reactions of the 1- and 2-butoxy radicals

The kinetics of the reactions of 1-and 2-butoxy radicals have been studied using a slow-flow photochemical reactor with GC-FID detection of reactants and products. Branching ratios between decomposition, CH3CH(O*)CH2CH3 --> CH3CHO + C2H5, reaction (7), and reaction with oxygen, CH3CH(O*)CH2CH3+ O2 --> CH3C(O)C2H5+ HO2, reaction (6), for the 2-butoxy radical and between isomerization, CH3CH2CH2CH2O* --> CH2CH2CH2CH2OH, reaction (9), and reaction with oxygen, CH3CH2CH2CH2O* + O2 --> C3H7CHO + HO2, reaction (8), for the 1-butoxy radical were measured as a function of oxygen concentration at atmospheric pressure over the temperature range 250-318 K. Evidence for the formation of a small fraction of chemically activated alkoxy radicals generated from the photolysis of alkyl nitrite precursors and from the exothermic reaction of 2-butyl peroxy radicals with NO was observed. The temperature dependence of the rate constant ratios for a thermalized system is given by k7/k6= 5.4 x 10(26) exp[(-47.4 +/- 2.8 kJ mol(-1))/RT] molecule cm(-3) and k9/k8= 1.98 x 10(23) exp[(-22.6 +/- 3.9 kJ mol(-1))/RT] molecule cm(-3). The results agree well with the available experimental literature data at ambient temperature but the temperature dependence of the rate constant ratios is weaker than in current recommendations.     

Low-energy paths for the unimolecular decomposition of CH3OH: a G2M/statistical theory study

The potential energy surface (PES) of the CH3OH system has been characterized by ab initio molecular orbital theory calculations at the G2M level of theory. The mechanisms for the decomposition of CH3OH and the related bimolecular reactions, CH3 + OH and 1CH2 + H2O, have been elucidated. The rate constants for these processes have been calculated using variational RRKM theory and compared with available experimental data. The total decomposition rate constants of CH3OH at the high- and low-pressure limits can be represented by k infinity = 1.56 x 10(16) exp(-44,310/T) s-1 and kAr0 = 1.60 x 10(36) T-12.2 exp(-48,140/T) cm3 molecule-1 s-1, respectively, covering the temperature range 1000-3000 K, in reasonable agreement with the experimental values. Our results indicate that the product branching ratios are strongly pressure dependent, with the production of CH3 + OH and 1CH2 + H2O dominant under high (P > 10(3) Torr) and low (P < 1 atm) pressures, respectively. For the bimolecular reaction of CH3 and OH, the total rate constant and the yields of 1CH2 + H2O and H2 + HCOH at lower pressures (P < 5 Torr) could be reasonably accounted for by the theory. For the reaction of 1CH2 with H2O, both the yield of CH3 + OH and the total rate constant could also be satisfactorily predicted theoretically. The production of 3CH2 + H2O by the singlet to triplet surface crossing, predicted to occur at 4.3 kcal mol-1 above the H2C...OH2 van der Waals complex (which lies 82.7 kcal mol-1 above CH3OH), was neglected in our calculations.     

High-temperature shock tube measurements of methyl radical decomposition

We have studied the two-channel thermal decomposition of methyl radicals in argon, involving the reactions CH3 + Ar --> CH + H2 + Ar (1a) and CH3 + Ar --> CH2 + H + Ar (1b), in shock tube experiments over the 2253-3527 K temperature range, at pressures between 0.7 and 4.2 atm. CH was monitored by continuous-wave, narrow-line-width laser absorption at 431.1311 nm. The collision-broadening coefficient for CH in argon, 2gamma(CH-Ar), was measured via repeated single-frequency experiments in the ethane pyrolysis system behind reflected shock waves. The measured 2gamma(CH-Ar) value and updated spectroscopic and molecular parameters were used to calculate the CH absorption coefficient at 431.1311 nm (23194.80 cm(-1)), which was then used to convert raw traces of fractional transmission to quantitative CH concentration time histories in the methyl decomposition experiments. The rate coefficient of reaction 1a was measured by monitoring CH radicals generated upon shock-heating highly dilute mixtures of ethane, C2H6, or methyl iodide, CH3I, in an argon bath. A detailed chemical kinetic mechanism was used to model the measured CH time histories. Within experimental uncertainty and scatter, no pressure dependence could be discerned in the rate coefficient of reaction 1a in the 0.7-4.2 atm pressure range. A least-squares, two-parameter fit of the current measurements, applicable between 2706 and 3527 K, gives k(1a) (cm(3) mol(-1) s(-1)) = 3.09 x 1015 exp[-40700/T (K)]. The rate coefficient of reaction 1b was determined by shock-heating dilute mixtures of C2H6 or CH3I and excess O2 in argon. During the course of reaction, OH radicals were monitored using the well-characterized R(1)(5) line of the OH A-X (0,0) band at 306.6871 nm (32606.52 cm(-1)). H atoms generated via reaction 1b rapidly react with O2, which is present in excess, forming OH. The OH traces are primarily sensitive to reaction 1b, reaction 9 (H + O2 --> OH + O) and reaction 10 (CH3 + O2 --> products), where the rate coefficients of reactions 9 and 10 are relatively well-established. No pressure dependence could be discerned for reaction 1b between 1.1 and 3.9 atm. A two-parameter, least-squares fit of the current data, valid over the 2253-2975 K temperature range, yields the rate expression k(1b) (cm(3) mol(-1) s(-1)) = 2.24 x 10(15) exp[-41600/T (K)]. Theoretical calculations carried out using a master equation/RRKM analysis fit the measurements reasonably well.     

甲烷与HO2反应的微观动力学研究

应用从头算方法和变分过渡态理论,在B3LYP/6-311+G^**方法下和300～2000K温度范围内研究甲烷与HO₂反应的微观动力学特性,得到由过渡态向反应物方向、向产物方向的能垒分别是11.83和102.90kJ/mol,理论计算正向反应速率常数与实验值之比为1.08～2.85,用此方法还可以预测没有实验数据的温度点反应的速率常数.     

Quantum chemical and theoretical kinetics study of the O(3P) + C2H2 reaction: a multistate process

The potential energy surfaces of the two lowest-lying triplet electronic surfaces 3A' and 3A' for the O(3P) + C2H2 reaction were theoretically reinvestigated, using various quantum chemical methods including CCSD(T), QCISD, CBS-QCI/APNO, CBS-QB3, G2M(CC,MP2), DFT-B3LYP and CASSCF. An efficient reaction pathway on the electronically excited 3A' surface resulting in H(2S) + HCCO(A2A') was newly identified and is predicted to play an important role at higher temperatures. The primary product distribution for the multistate multiwell reaction was then determined by RRKM statistical rate theory and weak-collision master equation analysis using the exact stochastic simulation method. Allowing for nonstatistical behavior of the internal rotation mode of the initial 3A' adducts, our computed primary-product distributions agree well with the available experimental results, i.e., ca. 80% H(2S) + HCCO(X2A' + A2A') and 20% CH2(X3B1) + CO(X1sigma+) independent of temperature and pressure over the wide 300-2000 K and 0-10 atm ranges. The thermal rate coefficient k(O + C2H2) at 200-2000 K was computed using multistate transition state theory: k(T) = 6.14 x 10(-15)T (1.28) exp(-1244 K/T) cm3 molecule(-1) s(-1); this expression, obtained after reducing the CBS-QCI/APNO ab initio entrance barriers by 0.5 kcal/mol, quasi-perfectly matches the experimental k(T) data over the entire 200-2000 K range, spanning 3 orders of magnitude.     

Theoretical study on the mechanism of the CH2F + NO2 reaction

Despite the importance of the Fluoromethyl radicals in combustion chemistry, very little experimental information on their reactions toward stable molecules is available in the literature. Motivated by recent laboratory characterization about the reaction kinetics of Chloromethyl radicals with NO2, we carried out a detailed potential energy survey on the CH2F + NO2 reaction at the B3LYP/6-311G(d,p) and MC-QCISD (single-point) levels as an attempt toward understanding the CH2F + NO2 reaction mechanism. It is shown that the CH2F radical can react with NO2 to barrierlessly generate adduct a (H2FCNO2), followed by isomerization to b1 (H2FCONO-trans) which can easily interconvert to b2 (H2FCONO-cis). Subsequently, Starting from b (b1, b2), the most feasible pathway is the C--F and N--O1 bonds cleavage along with N--F bond formation of b (b1, b2) leading to P1 (CH2O + FNO), or the direct N--O1 weak-bond fission of b (b1, b2) to give P2 (CH2FO + NO), or the 1,3-H-shift associated with N--O1 bond rupture of b1 to form P3 (CHFO + HNO), all of which may have comparable contribution to the reaction CH2F + NO2. Much less competitively, b2 either take the 1,4-H-shift and O1--N bond cleavage to form product P4 (CHFO + HON) or undergo a concerted H-shift to isomer c2 (HFCONOH), followed by dissociation to P4. Because the rate-determining transition state (TSab1) in the most competitive channels is only 0.3 kcal/mol higher than the reactants in energy, the CH2F + NO2 reaction is expected to be rapid, and may thus be expected to significantly contribute to elimination of nitrogen dioxide pollutants. The similarities and discrepancies among the CH2X + NO2 (X = H, F, and Cl) reactions are discussed in terms of the electronegativity of halogen atom. The present article may assist in future experimental identification of the product distributions for the title reaction, and may be helpful for understanding the halogenated methyl chemistry.