新型反相微乳液制备纳米结构甲烷催化燃烧催化剂La0.95Ba0.05MnAl11O19-α的研究

提出一种由水, 异丙醇, 正丁醇组成的新型微乳液, 并以其为反应介质制备了甲烷高温燃烧La_0.95Ba_0.05MnAl₁₁O_19-a催化剂. 采用¹H NMR, FT-IR, 电导法及激光粒度散射法研究了新型微乳液中水的结构及相特性. 新型微乳液中水的体积分数小于一定值时, 电导率与水含量成非线性关系, k～φ曲线上存在一临界值(φ^P＝0.15). 水质子的化学位移随水含量的降低移向高场. 加入4% D₂O测定的O—D键的伸缩振动随水含量增加而向高波数方向移动. 异丙醇铝在新型微乳液中水解形成的Al(OH)₃ 胶体粒子的粒径范围为226～329 nm. 采用新型微乳液作为反应介质制备的Ba_0.05La_0.95MnAl₁₁O_19-α催化剂的粒径在30 nm, 明显小于纯水制备的样品(100 nm). BET 比表面积为65 m²/g, 比纯水制备样品高出约一倍. XRD结果显示, 1200 ℃焙烧10 h即可获得含单一β-Al₂O₃相的催化剂. Ba_0.05La_0.95MnAl₁₁O_19-α催化剂甲烷催化燃烧的T₁₀为420 ℃, 比纯水制备样品下降了90 ℃. 甲烷催化燃烧活性提高是由于含有较多Mnⁿ+纳米结构六铝酸盐的形成.     

Synthesis of Pharmaceutical Intermediates by Toluene Benzylation over Heteropoly Acids on Different Support

Selective formation of pharmaceutical intermediates like diphenylmethane, dimethyl- diphenylmethane, benzyl toluene and benzoic acid by liquid phase, toluene benzylation with benzyl chloride as a benzylating agent, was systematically studied over plane clay (K-10, montmorillonite), plane H-Beta, plane MFI structured titanosilicate (TS-1) and heteropoly acids [HPA, namely dodeca-tungstophosphoric acid [H3PO4.12WO3.xH2O] (TPA), dodeca-molybdo phosphoric acid ammonium salt hydrate [H12Mo12N3O40P aq] (DMAA), sodium tungstate hydrated purified [Na12WO4.2H2O] (STH)] supported on clay, H-beta and TS-1. The 20%TPA/Clay, 30%TPA/H-Beta and 30%TPA/TS-l, were observed to be the best catalyst samples over plane clay, plane H-Beta and plane TS-1. The catalyst samples are compared with respect to benzyl chloride conversion and selectivities for diphenylmethane, dimethyl-diphenylmethane, benzyl toluene and benzoic acid. The reaction follows the pseudo-first order rate power law model. The apparent rate constants are calculated and compared with the reported ones.     

Effect of La2O3／γ—Al2O3 Catalyst on the Activation of CH4 and CO2 to C2 Hydrocarbons under Non—equilibrium Plasma

In the reaction of methane and carbon dioxide to C2 hydrocabons under non-equilibrium plasma, methane conversion was decreased,but selectivity of C2 hydroxarbons was increased when using La2O3/γ-Al2O3 as catalyst. So the yield of C2 hydrocarbons was higher than using plasma alone. The synergism of La2O3/γ-Al2O3 and plasma gave methane conversion of 24.9% and C2 yield of 18.1%. The distribution of C2 hydrocarbons changed when Pd-La2O3/γ-Al2O3 was used as catalyst,the major C2 product was ethylene.     

Structure and catalytic mechanism of methane monooxygenase and approaches to its modelling

The mechanisms of activation of O₂ and CH₄ by methane monooxygenase (MMO) are discussed. A new concept for the catalytic cycle of MMO is suggested, and approaches to its chemical modelling are considered.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 6, pp. 1011–1020, June, 1995.The author is grateful to Academician A. E. Shilov for interest in this work and helpful discussions. The work was financially supported by the Russian Foundation for Basic Research (Project No. 94-03-08529), International Scientific Foundation (Grant REU000), and INTAS (Project No. 93-315).     

Complete basis set ab initio computational study of ionization potential, electron affinity and the C-F bond dissociation energy for perfluorinated methane derivatives

A computational study of perfluorinated methane derivatives was performed with complete basis set ab initio methods. The total energies for their neutral, cation, and anionic states were computed. From these values, the energy gaps between different electronic states, ionization potentials, electron affinities, and C-F bond dissociation energies were calculated. The computed values are compared with experimental data and the reliability of complete basis set ab initio methods is discussed. New values for C-F bond dissociation energies are suggested. Received: 12 January 1998 / Accepted: 2 April 1998 / Published online: 29 July 1998     

The circular chemistry conceptual framework: A way forward to sustainability in industry 4.0

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Methane conversion to C2 hydrocarbons in solid electrolyte membrane reactors

Solid electrolyte membrane reactors (SEMRs) have been used to both study and influence catalytic reaction rates. Methane coupling is the reaction most thoroughly and intensively studied in these membrane reactors. In the last 20 years, oxygen ion (O²⁻), proton (H⁺) and mixed (O²⁻-e⁻, H⁺-e⁻) conducting membranes have been tested in order to maximize the conversion of methane to C₂ compounds. The present review contains the fundamental operating principles of the various SEMR types and their applications in this reaction. The difficulties that should be overcome in order to promote this SEMR process to an industrial scale are discussed.     

甲烷氧化偶联Ti-La-Li系多元氧化物催化剂的表面碱性和表面活性氧种

利用ＣＯ２－ＴＰＤ方法考察了Ｔｉ－Ｌａ－Ｌｉ系多元氧化物催化剂的表面碱性，实验发现：Ｃ２选择性与表面碱强度呈顺变关系，而ＣＨ４转化率与ＣＯ２的脱附峰面积呈顺变关系。同时，利用ＸＰＳ，Ｏ２－ＴＰＤ等方法对该体系催化剂的表面活性氧种进行了表征与研究。结果表明：催化剂的表面晶格氧与Ｃ２选择性有关，表面吸附氧与甲烷转化（包括偶联和深度氧化）有关。Ｏ２－ＴＰＤ实验发现催化剂的表面存在三种氧。α（１００℃≤ｔ     

CH4, CO2和H2O在非金属原子修饰石墨烯表面的吸附

煤层气(矿井瓦斯)是一种有望替代传统化石燃料，如煤、石油和天然气的非常规气体. 作为可得的清洁能源，它的利用被认为是节能和经济的选择. 在本工作中，非金属原子X(X=H，O，N，S，P，Si，F，Cl)修饰的石墨烯(Gr)被用来代表具有结构异性的煤表面模型. 通过密度泛函理论系统地研究了煤层气组分Y(Y=CH₄，CO₂，H₂O)在非金属原子修饰石墨烯上的吸附作用. 结果表明Y在非金属原子修饰石墨烯上的吸附均为物理吸附. 态密度和差分电荷密度共同表明了这种弱的相互作用.其中，H和Cl对CH₄的作用较大； N、O、F、Cl对CO₂的作用较强； N，Cl对H₂O的影响不容忽视. 总的来说，吸附能大小依次为：H₂O>CO₂>CH₄. 因此，在CH₄富集的煤层里注入H₂O或CO₂可以与CH₄形成竞争吸附，进而提高煤层气采收率. 本工作提供了在分子水平下煤层气与非金属原子修饰石墨烯之间的相互作用的详情，并为煤层瓦斯的开采与分离提供了有用的信息.     

Methanol Suppression of Trichloroethylene Degradation byMethylosinus trichosporium (OB3b) and Methane-Oxidizing Mixed Cultures

The effect of methanol on trichloroethylene (TCE) degradation by mixed and pure methylotrophic cultures was examined in batch culture experiments. Methanol was found to relieve growth inhibition ofMethylosinus trichosporium (OB3b) at high (14 mg/L) TCE concentrations. Degradation of TCE was determined by both radiolabeling and gas chromatography techniques. When cultures were grown on methanol over 10 to 14 d with 0.3 mg/L TCE, OB3b degraded 16.89 ±0.82% (mean± SD) of the TCE, and a mixed culture (DT type II) degraded 4.55±0.11%. Mixed culture (JS type I) degraded 4.34±0.06% of the TCE. When grown on methane with 0.3 mg/L TCE, 32.93±2.01% of the TCE was degraded by OB3b, whereas the JS culture degraded 24.3 ±1.38% of the TCE, and the DT culture degraded 34.3 ±2.97% of the TCE. The addition of methanol to cultures grown on methane reduced TCE degradation to 16.21 ±1.17% for OB3b and to 5.08±0.56% for JS. Although methanol reduces the toxicity of TCE to the cultures, biodegradation of TCE cannot be sustained in methanol-grown cultures. Since high TCE concentrations appear to inhibit methane uptake and growth, we suggest the primary toxicity of TCE is directed towards the methane monooxygenase.