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1.
The reaction of OH with acetylene was studied in a discharge flow system at room temperature. OH was generated by the reaction of atomic hydrogen with NO2 and was monitored throughout the reaction using ESR spectroscopy. Mass-spectrometric analysis of the reaction products yielded the following results: (1) less than 3 molecules of OH were consumed, and less than 2 molecules of H2O were formed for every molecule of acetylene that reacted; (2) CO was identified as the major carbon-containing product; (3) NO, formed in the generation of OH, reacted with a reaction intermediate to give among other products N2O. These observations placed severe limitations on the choice of a reaction mechanism. A mechanism containing the reaction OH + C2H2 → HC2O + H2 better accounted for the experimental results than one involving the abstraction reaction OH + C2H2 → C2H + H2O. The rate constant for the initial reaction was measured as 1.9 ± 0.6 × 10?13 cm3 molecule?1 sec?1.  相似文献   

2.
A new reforming process was studied using Ni/SiO2 with a hydrogen-permeating membrane reactor. Nickel catalyst supported on SiO2 is highly active for CH4-H2O-O2 reaction in membrane reactor and the reaction close to CH4 + 0.35O2 + 1.3H2O → CO2 + 3.3H2 proceeds at 873 K. Since the selectivity to carbon and CO2 increased and decreased with decreasing contact time respectively, it is considered that the reaction was started by decomposition of CH4 followed by oxidation of C and water shift reaction. Therefore, the reaction mechanism was different from so-called autothermal reforming (ATR) reaction.  相似文献   

3.
A new reforming process was studied using Ni/SiO2 with a hydrogen-permeating membrane reactor. Nickel catalyst supported on SiO2 is highly active for CH4?H2O?O2 reaction in membrane reactor and the reaction close to CH4+0.35O2+1.3H2O→CO2+3.3H2 proceeds at 873 K. Since the selectivity to carbon and CO2 increased and decreased with decreasing contact time respectively, it is considered that the reaction was started by decomposition of CH4 followed by oxidation of C and water shift reaction. Therefore, the reaction mechanism was different from so-called autothermal reforming (ATR) reaction.  相似文献   

4.
The insertion and abstraction reaction mechanisms of singlet and triplet CCl2 with CH3MH (M=O, S) have been studied by using the DFT, NBO and AIM methods. The geometries of reactions, the transition state and products were completely optimized by B3LYP/6–311G(d, p). All the energy of the species was obtained at the CCSD(T)/6–311G(d, p) level. The calculated results indicated that the major pathways of the reaction were obtained on the singlet potential energy surface. The singlet CCl2 can not only trigger the insertion reaction with C-H and M-H in four pathways, by which the products P1 [CH3OCHCl2, reaction I(1)], P3[Cl2HCCH2OH, reaction I(2)], P5[CH3SCHCl2, reaction II(1)] and P7[Cl2HCCH2SH, reaction II(2)] are produced respectively, but also abstract M-H, resulting P4 [CH2O+CH2Cl2, reaction I(3)] and P8[CH2S+CH2Cl2, reaction II(3)]. In addition, the important geometries in domain pathways have been studied by AIM and NBO theories. Supported by the National Natural Science Foundation of China (Grant No. 20335030) and Foundation of Education Committee of Gansu Province (Grant No. 0708-11)  相似文献   

5.
The dark reaction of NOx and H2O vapor in 1 atm of air was studied for the purpose of elucidating the recently discussed unknown radical source in smog chambers. Nitrous acid and nitric oxide were found to be formed by the reaction of NO2 and H2O in an evacuable and bakable smog chamber. No nitric acid was observed in the gas phase. The reaction is not stoichiometric and is thought to be a heterogeneous wall reaction. The reaction rate is first order with respect to NO2 and H2O, and the concentrations of HONO and NO initially increase linearly with time. The same reaction proceeds with a different rate constant in a quartz cell, and the reaction of NO2 and H218O gave H18ONO exclusively. Taking into consideration the heterogeneous reaction of NO2 and H2O, the upper limit of the rate constant of the third-order reaction NO + NO2 + H2O → 2HONO was deduced to be (3.0 ± 1.4) × 10?10 ppm?2-min?1, which is one order of magnitude smaller than the previously reported value. Nitrous acid formed by the heterogeneous dark reaction of NO2 and H2O should contribute significantly to both an initially present HONO and a continuous supply of OH radicals by photolysis in smog chamber experiments.  相似文献   

6.
应用密度泛函理论DFT/B3LYP对HO2+NO2反应进行了研究, 在B3LYP/6-311G**和CCSD(T)/6-311G**水平上计算了HO2自由基与NO2分子反应的单重态和三重态反应势能面, 计算结果表明, 单重态反应势能面中的直接氢抽提反应机理是此反应的主要反应通道, 即HO2自由基的氢原子转移到NO2分子的氮原子上形成产物P1 (HNO23O2), 另一个可能的反应通道是单重态反应势能面上HO2中的端位氧原子进攻NO2分子中的氮原子形成中间体1 (HOONO2), 接着中间体1 (HOONO2)经过氢转移形成产物P2 (trans-HONO+3O2), 以上两个反应通道都是放热反应通道, 分别放热90.14和132.52 kJ•mol-1.  相似文献   

7.
The hydroformylation of acrylonitrile (VCN) using Co2(CO)8/L (L  HN(CH2CN)2, H2C(CH2)3NMe, Me2N(CH2)2NMeH, PPh3, and PCy3) has been examined in methanol solvent. Four reaction pathways are observed which are dependent on L. With no L or with L  HN(CH2CN)2, the reaction produces the desired acetal (MeO)2CHCH2CH2CN. For the more basic amines the reaction produces ~ 50% yields of hydrodimerization products NCCHMe(CH2)2CN/NC(CH2)4CN in a 10/1 ratio and an ~ 30% yield of the hydrogenation product CH3CH2CN. These reactions are shown to be metal catalyzed. The main reaction for Co2(CO)8/PR3 catalyzed systems appears to be a classical Michael addition reaction of the solvent, methanol, with acrylonitrile to give MeOCH2CH2CN. Evidence is given to show that this reaction is catalyzed by phosphine which has dissociated under reaction conditions and not by a ligated cobalt complex.  相似文献   

8.
The bimolecular single collision reaction potential energy surface of CN radical with ketene (CH2CO) was investigated by means of B3LYP and QCISD(T) methods. The calculated results indicate that there are three possible channels in the reaction. The first is an attack reaction by the carbon atom of CN at the carbon atom of the methylene of CH2CO to form the intermediate NCCH2CO followed by a rupture reaction of the C-C bond combined with -CO group to the products CH2CN CO. The second is a direct addition reaction between CN and CH2CO to form the intermediate CH2C(O)CN followed by its isomerization into NCCH2CO via a CN-shift reaction, and subsequently, NCCH2CO dissociates into CH2CN CO through a CO-loss reaction. The last is a direct hydrogen abstraction reaction of CH2CO by CN radical. Because of the existence of a 15.44 kJ/mol reaction barrier and higher energy of reaction products, the path can be ruled out as an important channel in the reaction kinetics. The present theoretical computation results, which give an available suggestion on the reaction mechanism, are in good agreement with previous experimental studies.  相似文献   

9.
Kinetics of reaction between Na2S203 and peroxide compound (H202 or Na2S2O3) in a batch reactor and in a continuous stirring tank reactor (CSTR) were studied. Steady oscillations in uncatalyzed reactions in a CSTR were first discovered. In Na2S203-H2O2-H2S04 reaction system, Pt potential and pH of higher and lower flow rates beyond oscillation flow rates were in around the same extreme values. The reaction catalyzed by Cu2+ consists of the catalyzed oscillation process and the uncatalyzed osciliation one. On the basis of experiment, a reaction mechanism consisting of three stages was put forward. The three stages are H+ positive-feedback reactions, proton negative-feedback (uncatalyzed negative-feedback and catalyzed negative-feedback) reactions and transitional reactions. The mechanism is able to explain reasonably the nonlinear chemical phenomena appearing in the thiosulfate oxidation reaction by peroxide compounds. Project supported by the National Natural Science Foundation of China.  相似文献   

10.
Our groups studies on Cu/ZnO-based catalysts for methanol synthesis via hydrogenation of CO2 and for the water-gas shift reaction are reviewed. Effects of ZnO contained in supported Cu-based catalysts on their activities for several reactions were investigated. The addition of ZnO to Cu-based catalyst supported on Al2O3, ZrO2 or SiO2 improved its specific activity for methanol synthesis and the reverse water-gas shift reaction, but did not improve its specific activity for methanol steam reforming and the water-gas shift reaction. Methanol synthesis from CO2 and H2 over Cu/ZnO-based catalysts was extensively studied under a joint research project between National Institute for Resources and Environment (NIRE; one of the former research institutes reorganized to AIST) and Research Institute of Innovative Technology for the Earth (RITE). It was suggested that methanol should be produced via the hydrogenation of CO2, but not via the hydrogenation of CO, and that H2O produced along with methanol should greatly suppress methanol synthesis. The Cu/ZnO-based multicomponent catalysts such as Cu/ZnO/ZrO2/Al2O3 and Cu/ZnO/ZrO2/Al2O3/Ga2O3 were highly active for methanol synthesis from CO2 and H2. The addition of a small amount of colloidal silica to the multicomponent catalysts greatly improved their long-term stability during methanol synthesis from CO2 and H2. The purity of the crude methanol produced in a bench plant was 99.9 wt% and higher than that of the crude methanol from a commercial methanol synthesis from syngas. The water-gas shift reaction over Cu/ZnO-based catalysts was also studied. The activity of Cu/ZnO/ZrO2/Al2O3 catalyst for the water-gas shift reaction at 523 K was less affected by the pre-treatments such as calcination and treatment in H2 at high temperatures than that of the Cu/ZnO/Al2O3 catalyst. Accordingly, the Cu/ZnO/ZrO2/Al2O3 catalyst was considered to be more suitable for practical use for the water-gas shift reaction. The Cu/ZnO/ZrO2/Al2O3 catalyst was also highly active for the water-gas shift reaction at 673 K. Furthermore, a two-stage reaction system composed of the first reaction zone for the water-gas shift reaction at 673 K and the second reaction zone for the reaction at 523 K was found to be more efficient than a one-stage reaction system. The addition of a small amount of colloidal silica to a Cu/ZnO-based catalyst greatly improved its long-term stability in the water-gas shift reaction in a similar manner as in methanol synthesis from CO2 and H2.  相似文献   

11.
Reaction of Adipic Acid Diamide with Phosphorus Pentachloride The reaction of adipamide (I) with phosphorus pentachloride in a solvent leads to (Cl3P?NCCl2CCl2CH2)2 (II). The stages of the reaction are: 1. chlorination of the keto and methylen groups 2. formation of the ? N?PCl3 group. This result is a supplement of the existing conception about the course of the reaction of carboxylic acid amides with phosphorus pentachloride. The reaction of (I) with PCl5 without any solvent has been reproduced and the course of reaction has also been investigated. This reaction gives mainly NC(CH2)4CN. The resulting product of a careful hydrolysis of (II) is (Cl2OPN?CClCl2CH2)2. A total hydrolysis gives back (I).  相似文献   

12.
在aug-cc-pVTZ基组下采用CCSD(T)和B3LYP方法,研究了H2O2+Cl反应,并考虑在大气中单个水分子对该反应的影响.结果表明,H2O2+Cl反应只存在一条生成产物为HO2+HCl的通道,其表观活化能为10.21kJ·mol-1.加入一分子水后,H2O2+Cl反应的产物并没有发生改变,但是所得势能面却比裸反应复杂得多,经历了RW1、RW2和RW3三条通道.水分子在通道RW1和RW2中对产物生成能垒的降低起显著的负催化作用,而在通道RW3中则起明显的正催化作用.利用经典过渡态理论(TST)并结合Wigner矫正模型计算了216.7-298.2 K温度范围内标题反应的速率常数.结果显示,298.2 K时通道R1的速率常数为1.60×10-13cm3·molecule-1·s-1,与所测实验值非常接近.此外,尽管通道RW3的速率常数kRW3比对应裸反应的速率常数kR1大了46.6-131倍,但该通道的有效速率常数k'RW3却比kR1小了10-14个数量级,表明在实际大气环境中水分子对H2O2+Cl反应几乎没有影响.  相似文献   

13.
The potential energy profile for the F+(H2O)3→HF+(H2O)2OH reaction has been investigated using the “gold standard” CCSD(T) method with correlation‐consistent basis sets up to cc‐pVQZ. Four different reaction pathways have been found and these are related, both geometrically and energetically. The entrance complexes F???(H2O)3 for all four reaction pathways are found lying ca. 7 kcal mol?1 below the separated reactants F+(H2O)3. The four reaction barriers on their respective reaction coordinates lie ca. 4 kcal mol?1 below the reactants. There are also corresponding exit complexes HF???(H2O)2OH, lying about 13 kcal mol?1 below the separated products HF+(H2O)2OH. Compared with analogous F+(H2O)2 and F+H2O reactions, the F+(H2O)3 reaction is somewhat similar to the former but qualitatively different from the latter. It may be reasonable to predict that the reactions between atomic fluorine and water tetramer (or even larger water clusters) may be similar to the F+(H2O)3 reaction.  相似文献   

14.
金国杰  郭杨龙  刘晓晖  姚伟  郭耘  卢冠忠 《化学学报》2006,64(19):1941-1946
制备了对丙烯直接气相环氧化具有优良催化性能的Ag-MoO3/ZrO2催化剂, 采用原位FT-IR技术研究了丙烯、环氧丙烷及丙烯和氧气混合气在载体和催化剂上的吸附及反应行为. 研究表明, 丙烯在ZrO2载体和20%Ag-4%MoO3/ZrO2催化剂上吸附后, 均不发生化学反应, 而环氧丙烷在ZrO2载体上吸附后于400 ℃发生开环反应, 在20%Ag-4%MoO3/ZrO2催化剂上吸附后于300 ℃发生开环反应. 当丙烯和氧气混合气在ZrO2载体上共吸附后, 随着反应温度从室温升高至400 ℃, 二者开始反应生成CO2和H2O; 混合气在20%Ag-4%MoO3/ZrO2催化剂上共吸附后于350 ℃开始反应. 对比非负载型Ag-MoO3催化剂的研究结果可见, ZrO2载体的存在使催化剂的活性下降的同时, 提高了对产物环氧丙烷的选择性.  相似文献   

15.
Degradation of methyl tert-butyl ether (MTBE) with Fe2+/H2O2 was studied by purge-and-trap gas chromatography-mass spectrometry. MTBE was degraded 99% within 120 min under optimum conditions. MTBE was firstly degraded rapidly based on a Fe2+/H2O2 reaction and then relatively slower based on a Fe3+/H2O2 reaction. The dissolved oxygen decreased rapidly in the Fe2+/H2O2 reaction stage, but showed a slow increase in the Fe3+/H2O2 reaction stage. tert-Butyl formate, tert-butyl alcohol, methyl acetate and acetone were identified as primary degradation products by mass spectrometry. A preliminary reaction mechanism involving two different pathways for the degradation of MTBE with Fe2+/H2O2 was proposed. This study suggests that degradation of MTBE can be achieved using the Fe2+/H2O2 process.  相似文献   

16.
高硅 Na-ZSM-5 分子筛表面 NO 的常温吸附-氧化机理   总被引:1,自引:0,他引:1  
刘华彦  张泽凯  徐媛媛  陈银飞  李希 《催化学报》2010,31(10):1233-1241
 采用程序升温表面反应 (TPSR) 和原位漫反射红外光谱 (DRIFTS) 等手段研究了常温下 NO 和 O2 在高硅 Na-ZSM-5 分子筛上吸附-氧化反应机理. 结果表明, Na-ZSM-5 分子筛上 NO 的催化氧化过程中伴随着显著的 NO2 物理吸附, 表现为 NO 氧化和 NO2 吸附间的动态平衡. Na-ZSM-5 分子筛表面 NOx 吸附物种的 TPSR 和原位 DRIFTS 表征表明, 化学吸附的 NO 和气相中的 O2  在 Na-ZSM-5 表面反应生成吸附态的 NO3, 并继续与 NO 作用生成弱吸附的 NO2  和 N2 O4, 它们吸附饱和后释放出来; 其中, 强吸附的 NO3 在 NO 氧化过程中起到了反应中间体的作用, 同时也促进了 NO 的吸附.  相似文献   

17.
The reaction of CuSO4 with Cu2SO2 to give Cu2SO4 was studied. The influence of the degree of reaction, the initial mixture composition and the temperature upon the reaction rate and the product composition was discussed. It was found that the reaction starts above 710 K and pure Cu2SO4 can be obtained under strictly defined conditions.  相似文献   

18.
深入理解辐照条件下氢同位素与CO2反应的微观机制,可为聚变堆氘氚燃料循环工艺的优化设计提供数据支撑。基于此,采用第一性原理计算研究了等离子体放电条件下H2和CO2的微观反应机制,研究了不同温度和氢同位素效应对反应过程的影响。通过内禀反应坐标(IRC)算法结合反应过渡态获得4条初始反应路径,并对比研究了生成产物CH4及CH3OH的2条路径在热力学上的容易程度,以及不同氢同位素对各个反应的影响。研究发现,氚的自发衰变或等离子体中的高能电子都会诱导氢同位素与CO2发生反应,形成CO、H2O、CH4及CH3OH等产物;在高能电子诱导CO2的离解后,由4条初始反应路径组成的复杂反应可以自持发生,且该复杂反应中存在2种倾向;升高反应温度对CO2转化为有机物(CH4和CH3OH)具有一定的促进作用。  相似文献   

19.
{Na(OCH3)[H3N(CH2)2NH2]2}[WO2(C10H6O2)2] (1) was obtained by the reaction of Na2WO4 · 2H2O with 2,3-dihydroxynaphthalene and ethylenediamine. [H2N(CH2)3NH3]2[WO2(C10H6O2)2] (2) was synthesized by the reaction of Na2WO4 · 2H2O with 2,3-dihydroxynaphthalene and 1,3-propylenediamine. Complex 1 was a one-dimensional chain-like structure and the Na atom is in the structure, while complex 2 was a discrete monomer without Na in its structure. The two complexes were synthesized in the same reaction conditions, except that protonated ethylenediamine was used in reaction 1, but 1,3-propylenediamine in reaction 2.  相似文献   

20.
The reactions between strontium and iron nitrates have been studied in an open atmosphere system using three different molar ratios, 1:1 (I), 1:2 (II) and 2:1 (III) at different temperatures as pointed out from the DTA data. The reaction mechanism was discussed based on the chemical composition characterized by means of thermal analysis, X‐ray diffraction patterns, infrared spectra and magnetic susceptibility. It was found that the reaction products depend on both temperature of reaction and the ratio between reactants. The reaction products were found to be composed of a variety of iron compounds that possess different valences: SrFeO2.86, SrFeO2.97, SrFe2O4, SrFe12O19, Sr2Fe2O5 and Sr7Fe10O22 in addition to some accessory reaction products namely α‐Fe2O3 and FeO(OH).  相似文献   

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