N2O分解反应的蒙特卡罗模拟

N2O作为大气污染物之一早已受到人们的注意，许多人研究了N2O在金属氧化物上的分解反应得到了一些基本的实验事实[1]：（1）反应速率与原料气中N2O的分压近似成比例．(2)在反应初期，N2的生成速率由大变小，O2的生成速率由小变大，达到平衡时，N2生成速率是O2生成速率的二倍．(3)过渡应答法研究表明，把原料气由N2O和He的混合气体切换成纯He后，N2立即停止发生，而O2的生成仍能维持一段时间．基于上述实验事实，人们对Nzo的催化分解反应提出了一些可能的机理，主要有下面两种看法：另一方面，人们还发现几O的催化分解反应是一个振荡…     

N2O分解反应中复杂动力学行为的模拟

在多相催化反应中，自ZO多年前第一次在实验中观察到反应的振荡现象以来，现已发现在许多催化反应中都存在振荡现象山．N。O分解是一个振荡反应问．我们在用MonteCarloMC）方法研究N20分解反应机理时，曾发现反应速率和表面覆盖度在一定条件下都会出现振荡现象＊．非统性理论的研究表明，体系内部只要存在非线性的相互作用就可能表现出一些复杂的动力学行为，如振荡和混饨等．N。O分解反应中的振荡行为，也是由于体系内部非线性相互作用的结果·本文用非线性动力学的方法研究N。O分解反应中表面氧覆盖度的振荡行为，发现振荡在一定条…     

不同离子影响下UV/Fenton试剂协同降解曙红B的研究

近年来,利用光催化氧化法降解难处理有机物是环境科学研究的热点问题之一。其中UV/Fenton反应已经被证明是一种有效处理有机废水的方法[1-3],其反应机理[4-7]和动力学研究[8]也被国内外广泛研究。紫外光和Fe2 对H2O2的催化分解具有协同效应,使H2O2的分解速率远大于Fe2 或紫外(UV)催化H2O2分解速率的简单加合,同时Fe2 在反应中得以再生,降低了Fe2 的用量,并保持了H2O2较高的利用率,与其他高级氧化技术(AOPs)相比,因其操作简单,反应快速,可产生絮凝,无二次污染等优点而倍受青睐。染料废水不仅具有水量大、成分复杂、COD值高、可生化…     

N2O的催化分解研究

N2O是主要的温室气体之一,它在对流层中具有破坏臭氧的作用,因此,N2O的消除越来越引起人们的重视。N2O的直接催化分解是公认的消除N2O污染的最有前景的方法之一,具有操作简单、成本低、不需引入其他杂质、不产生二次污染等特点。本文综述了近年来在N2O催化分解领域广受关注的几类催化剂的最新研究进展,包括金属氧化物催化剂、负载型贵金属催化剂和分子筛催化剂体系,概括了这些催化剂的优点和缺点,介绍了固体催化剂表面N2O催化分解的反应动力学、分子模拟及反应机理。从工业应用角度出发综述了工业生产过程中可能对催化活性造成影响的NOx、O2、H2O和SO2等其他气体对催化剂活性、寿命和稳定性的影响。最后指出了N2O催化分解理论研究及催化剂体系存在的一些问题,并在此基础上对N2O催化分解体系的发展前景进行了展望。     

氨基羧酸铁(III)配合物催化分解过氧化氢

用碘量法研究了[Fe（EDTA],[FeⅢ(DCTA)],[FeⅢ(EGTA)]催化分解H2O2反应，提出了反应动力学方程为-d[H2O2]/dt=k[FE(Ⅲ)][H2O2][H ]^-1，认为氨基羧酸铁（Ⅲ）配合物催化分解H2O2反应为键式自由基反应，反应中间体包括过氧铁（Ⅲ）配合物，氨基羧酸铁（Ⅱ）和HO-，HO2-自由基。     

Salen Mn（Ⅲ）配合物的合成及其在离子液体中对苯乙烯环氧化反应的催化性能

合成了在5,5’位上分别含羟基叔胺基和酯基叔胺基取代基的新型手性水杨醛Schiff碱的Salen Mn（Ⅲ）配合物1～4．在CH2Cl2／H2O反应体系中,以吡啶氮氧化物（PyNO）为助催化剂,NaCl0为氧化剂,考察了配合物1—4对苯乙烯环氧化的催化性能．以氯化-双[3-（叔丁基）-5-（N,N-二（乙醇基）氨基亚甲基）水杨醛]缩（1r,2R）-二苯基乙二胺[N,N’,O,O’]锰（Ⅲ）2和氯化-双[3-（叔丁基）-5-（N,N-二（乙酰乙酯基）氨基亚甲基）水杨醛]缩（1R,2R）-二苯基乙二胺[N,N’,O,O’]锰（11I）4为例,研究了不同的离子液体[BMIM]PF6和[BMIM]BF4对苯乙烯环氧化反应的影响．结果显示,两种离子液体的加入均能使催化剂循环使用,在离子液体[BMIM]PF。中,配合物2和4催化得到的环氧化物ee％值分别为53．2％和55．8％,且催化剂可以重复使用四次,效果好于在离子液体[BMIM]BF4中对苯乙烯的催化的影响．     

Pt/TiO2光催化分解四硼酸钾水溶液制氢

研究了以四硼酸钾溶液作反应体系，在1%Pt／TiO2光催化剂的作用下光催化分解水制氢的反应，发现该体系能使放氢速率明显提高．放氢速率还随B4O7^2-浓度的增大而增大．在此基础上，还对B4O7^2-的作用机理进行了探讨，BRO7^2-在该反应体系中主要是通过物理作用有效的阻止了逆反应的发生，从而使放氢速率得以提高．     

燃煤固硫及催化燃烧一体化添加剂的催化作用机理研究

用热重法研究了燃煤固硫及催化燃烧一体化添加剂对峰峰烟煤的催化燃烧和催化固硫作用，采用非等温燃烧反应模型和粒子模型，计算了加入一体化添加剂前后煤的燃烧反应动力学和固硫反应动力学参数，对一体化添加剂的催化作用机理进行了分析。结果表明，一体化添加剂中金属催化组分Fe2O3对煤的燃烧和固硫组分CaO的固硫均起到了较好的催化促进作用。一体化添加剂的加入可提高煤的燃烧反应速率，外加金属离子通过电荷迁移使碳表面的棱、角、缺陷等活性部位增加，加快了氧气的吸附速度，使反应活化能和频率因子降低。在燃烧固硫反应，一体化添加剂中金属助剂Fe2O3催化了SO2转变为SO3的过程，使固硫组分CaO的硫酸盐化反应表面化学反应速度常数k和有效扩散系数D增大，在固硫反应的产物层扩散控制阶段，Fe2O3的存在使得CaO晶粒团之间相互接触黏连的几率减小，减轻了固硫产物CaSO4的团聚，弱化了扩散作用的影响，减轻了CaO固硫反应的孔窒息效应。     

Ag_2~-催化CO氧化反应机理的理论研究

用密度泛函理论B3LYP方法详细研究了Ag_2~-催化CO氧化反应的机理.计算结果表明,O2分子在Ag_2~-和Au_2~-上吸附能相差不大,而CO分子在Ag_2~-上吸附要比在Ag_2~-上弱得多.Ag_2~-催化CO氧化反应共有四条反应途径.最可能反应通道为CO插入Ag2O_2~-中的Ag—O键形成中间体[Ag—AgC(O—O)O]-,然后直接分解形成产物CO2和Ag2O-,或另一分子CO进攻中间体[Ag—AgC(O—O)O]-形成两分子产物CO2和Ag_2~-.在动力学上最难进行的反应通道为经历碳酸根双银中间体,需要克服约0.24eV的能垒.Ag_2~-催化CO氧化反应活性要高于Au_2~-.     

Development of a certified reference material of nitrous oxide in nitrogen for emission gas measurement

A reference gas mixture of nitrous oxide (N₂O) in nitrogen, filled in a 10-L high-pressure aluminum alloy gas cylinder, has been developed as a certified reference material for emission measurement of exhaust gases from automobiles. As an example of certified values, mole fraction of N₂O is 302.36 μmol/mol. An electronic mass comparator with a home-made automatic cylinder exchanger, gas-filling equipment, and a gas chromatograph with a thermal conductivity detector have been used for the production of this CRM. The gas chromatographic analysis has of sufficient precision. The mole fraction of N₂O has good long-term stability for 10 years and is independent of inner pressure in the gas cylinder. As these results, a relative expanded uncertainty (coverage factor is 2) of the certified value has become 0.28 %. This sufficiently small uncertainty of the N₂O mole fraction will be advantageous in the calibration of analytical instruments for emission gas analysis.     

MONTE CARLO SIMULATION OF THE SURFACE REDOXMECHANISM OF WATER GAS SHIFT REACTION 2. KINETICS OF FORWARD WATER GAS SHIFT REACTION

IntroductionThewatergasshift(WGS)reaction,duetoitsimportanceinbothhydrogenproductionandenergytechnology,hasbeenwidelyinvestigated.Inourpreviousworkll],aMonteCarlomodelwasdevelopedtoinvestigatetheconversionofOH*toO*inthesuifaceredoxmechamsmofWGSreaction,an…     

Experimental study and detailed modeling of toluene degradation in a low-pressure stoichiometric premixed CH4/O2/N2 flame

Temperature and mole fraction profiles have been measured in laminar stoichiometric premixed CH4/O2/N2 and CH4/1.5%C6H5CH3/O2/N2 flames at low pressure (0.0519 bar) by using thermocouple, molecular beam/mass spectrometry (MB/MS), and gas chromatography/mass spectrometry (GC/MS) techniques. The present study completes our previous work performed on the thermal degradation of benzene in CH4/O2/N2 operating at similar conditions. Mole fraction profiles of reactants, final products, and reactive and stable intermediate species have been analyzed. The main intermediate aromatic species analyzed in the methane-toluene flame were benzene, phenol, ethylbenzene, benzylalcohol, styrene, and benzaldehyde. These new experimental results have been modeled with our previous model including submechanisms for aromatics (benzene up to p-xylene) and aliphatic (C1 up to C7) oxidation. Good agreement has been observed for the main species analyzed. The main reaction paths governing the degradation of toluene in the methane flame were identified, and it occurs mainly via the formation of benzene (C6H5CH3 + H = C6H6 + CH3) and benzyl radical (C6H5CH3 + H = C6H5CH2 + H2). Due to the abundance of methyl radicals, it was observed that recombination of benzyl and methyl is responsible for main monosubstitute aromatic species analyzed in the methane-toluene flame. The oxidation of these substitute species led to cyclopentadienyl radical as observed in a methane-benzene flame.     

苦味酸碳酰肼、苦味酸氨基脲和苦味酸氨基胍的温度跃升傅里叶变换红外光谱

利用温度跃升傅里叶变换红外原位分析技术(T-jump/FTIR)对苦味酸碳酰肼,苦味酸氨基脲和苦味酸氨基胍的快速热分解过程进行了研究,利用快速扫描傅里叶变换红外光谱在线检测气相产物的种类及浓度变化趋势。研究发现,在0.1 MPa氩气气氛下,这3种化合物快速热分解过程的含氮气相产物主要有NO、NH3、HCN、NO2、HONO和HNCO,含碳气相产物主要有CO2、CO、HCN、HNCO和HONO,NH3可进一步氧化为NO2,N2O和H2O等产物;实验同时得到了快速热分解主要气相产物摩尔分数随时间的变化关系曲线。研究表明,苦味酸氨基脲作为新型、安全、环保起爆药剂和汽车安全气囊产气剂组分有很好的发展前景。     

Interaction of oxygen with TiN(001): N<-->O exchange and oxidation process

This work presents a detailed experimental and theoretical study of the oxidation of TiN(001) using a combination of synchrotron-based photoemission and density functional theory (DFT). Experimentally, the adsorption of O2 on TiN(001) was investigated at temperatures between 250 and 450 K. At the lowest temperature, there was chemisorption of oxygen (O(2,gas)-->2O(ads)) without significant surface oxidation. In contrast, at 450 K the amount of O2 adsorbed increased continuously, there was no evidence for an oxygen saturation coverage, a clear signal in the Ti 2p core level spectra denoted the presence of TiOx species, and desorption of both N2 and NO was detected. The DFT calculations show that the adsorption/dissociation of O2 is highly exothermic on a TiN(001) substrate and is carried out mainly by the Ti centers. A high oxygen coverage (larger than 0.5 ML) may induce some structural reconstructions of the surface. The exchange of a surface N atom by an O adatom is a highly endothermic process (DeltaE=2.84 eV). However, the overall oxidation of the surface layer is thermodynamically favored due to the energy released by the dissociative adsorption of O2 and the formation of N2 or NO. Both experimental and theoretical results lead to conclude that a TiN+mO2 -->TiOx + NO reaction is an important exit channel for nitrogen in the oxidation process.     

2-(氨基苯基)六氟异丙醇衍生物的合成

以六氟丙酮三水合物和芳香胺为原料,合成了一系列2-芳胺基六氟异丙醇化合物。研究了反应中原料配比、催化剂种类及用量、溶剂种类、反应时间及取代基对反应的影响。结果表明,在六氟丙酮三水合物用量为90 mmol,芳香胺用量为30 mmol,对甲基苯磺酸为催化剂,其用量为苯胺物质量的6%时,回流反应5～35h,反应的转化率和收率分别高达40.1%～100.0%,39.0%～99.0%。同时本文对六氟丙酮三水合物和无水六氟丙酮与苯胺的反应机理进行了比较,推测了六氟丙酮三水合物与苯胺的反应历程,并通过对其中间产物结构的表征进一步确认了该历程。     

On the chemical kinetics of n-butanol: ignition and speciation studies

Direct measurements of intermediates of ignition are challenging experimental objectives, yet such measurements are critical for understanding fuel decomposition and oxidation pathways. This work presents experimental results, obtained using the University of Michigan Rapid Compression Facility, of ignition delay times and intermediates formed during the ignition of n-butanol. Ignition delay times for stoichiometric n-butanol/O(2) mixtures with an inert/O(2) ratio of 5.64 were measured over a temperature range of 920-1040 K and a pressure range of 2.86-3.35 atm and were compared to those predicted by the recent reaction mechanism developed by Black et al. (Combust. Flame 2010, 157, 363-373). There is excellent agreement between the experimental results and model predictions for ignition delay time, within 20% over the entire temperature range tested. Further, high-speed gas sampling and gas chromatography techniques were used to acquire and analyze gas samples of intermediate species during the ignition delay of stoichiometric n-butanol/O(2) (χ(n-but) = 0.025, χ(O(2)) = 0.147, χ(N(2)) = 0.541, χ(Ar) = 0.288) mixtures at P = 3.25 atm and T = 975 K. Quantitative measurements of mole fraction time histories of methane, carbon monoxide, ethene, propene, acetaldehyde, n-butyraldehyde, 1-butene and n-butanol were compared with model predictions using the Black et al. mechanism. In general, the predicted trends for species concentrations are consistent with measurements. Sensitivity analyses and rate of production analyses were used to identify reactions important for predicting ignition delay time and the intermediate species time histories. Modifications to the mechanism by Black et al. were explored based on recent contributions to the literature on the rate constant for the key reaction, n-butanol+OH. The results improve the model agreement with some species; however, the comparison also indicates some reaction pathways, particularly those important to ethene formation and removal, are not well captured.     

Effect of co-adsorbed CO and reaction temperature on the dynamics of N2 desorption under steady-state N2O-CO reaction on Rh(110)

We have investigated the effect of co-absorbed CO and reaction temperature on the angular distribution of N(2) desorption by N(2)O decomposition under the steady state of N(2)O-CO reaction on Rh(110). Spatial distributions of desorbing product N(2) emission have been measured at various surface temperatures and CO coverages. The decomposed N(2) collimates at 48°-61° off normal in the parallel plane to [001] and [110] directions, indicating that adsorbed N(2)O just before the decomposition is oriented along the [001] direction. Although the inclined and collimated N(2) desorption is always observed at any steady-state CO coverage and reaction temperature, the shape of the collimated N(2) distribution varied dependent on the co-adsorbed CO coverage. The distribution becomes sharp and shifts toward the surface normal direction with increasing CO coverage. These effects of adsorbed CO on the angular distribution of N(2) are interpreted by the collision of desorbed N(2) with co-adsorbed CO.     

二-（2-乙基己基）磷酸P204与三烷基叔胺N235协同萃取钼

研究了P204（二-(2-乙基己基)磷酸, HA）和N235（三烷基胺, R3N）二元体系在HCl介质中对金属钼的萃取,结果表明P204和N235混合萃取剂在萃取钼时存在协同效应,并且在N235摩尔分数为0.7时协萃系数为2.24;考察了溶液酸度、P204或N235浓度及温度对萃取钼的影响,确定了协萃络合物为(R3NH)3•HMo8O26•2(HA),并比较了负载前后有机相的红外光谱。     

Quantitative analyses of shape-selective intercalation of isomeric mixtures of muconates into [LiAl2(OH)6]Cl.yH2O layered double hydroxide

Quantitative investigation of the shape selectivity for the competitive intercalation reaction of isomeric mixtures in the interlayer of LDH was achieved by analyzing the solid phases synthesized by the reaction of [LiAl(2)(OH)(6)]Cl.yH(2)O with various compositional mixtures of (E,E)- and (Z,Z)-muconates. The apparent partition constant K' for the anion-exchange reaction between (E,E)- and (Z,Z)-muconates was quite dependent on the mole fraction of muconates in solution. The only single phase saturated with [LiAl(2)(OH)(6)](2)[(E,E)-C(6)H(4)O(4)].zH(2)O could be obtained in the range of the initial mole fraction of (E,E)-muconate larger than 0.6 in the starting solution, while mixed phases intercalated with (E,E)- and (Z,Z)-muconates could be obtained at lower mole fractions of (E,E)-muconate. The shape selectivity for the competitive reaction of two muconates on the [LiAl(2)(OH)(6)](+) lattice could be ascribed to thermodynamic processes, and the conditions under which that pure (E,E)-muconate was efficiently separated from isomeric mixtures of two muconates were successfully evaluated.