激光诱导二甲基二乙氧基硅烷气相合成碳化硅超细粉

本工作首次采用有机硅试剂二甲基二乙氧基硅烷为反应物，进行了激光导气相反应，制备出平均粒径为４０ｎｍ的非晶ＳｉＣ粉末，粉末中Ｃ／Ｓｉ比随反应气流量的变化而变化。非晶ＳｉＣ粉末在１８７３Ｋ，氮气中退火１ｈ后转变为β－ＳｉＣ及α－ＳｉＣ，同时，粉末中部分氧杂质及自由碳脱出粉末。     

Synthesis of Dimethyl Carbonate from Methanol and Carbon dioxide using Potassium Methoxide as Catalyst under Mild Conditions

Pd-supported on WO₃–ZrO₂ (W/Zr atomic ratio=0.2) calcined at 1073 K was found to be highly active and selective for gas-phase oxidation of ethylene to acetic acid in the presence of water at 423 K and 0.6 MPa. Contact time dependence demonstrated that acetic acid is formed via acetaldehyde formed by a Wacker-type reaction, not through ethanol by hydration of ethylene.     

Ce和La改性固体超强酸S2O82-/ZrO2-SiO2催化剂合成及其酯化性能研究

以Zr(NO₃)₄·5H₂O和Na₂SiO₃·9H₂O为原料,利用共沉淀法制备前驱体,浸渍添加稀土Ce和La,一定温度焙烧后制得掺杂稀土S₂O₈^2-/ZrO₂-SiO₂固体超强酸。通过XRD、FT-IR和SEM对催化剂进行表征,以硬脂酸的酯化合成反应为探针,考察制备条件对催化剂性能的影响以及催化剂的重复使用率。结果表明,相对于未改性的S₂O₈^2-/ZrO₂-SiO₂催化剂,添加了Ce或La的固体超强酸酯化催化活性及重复使用性能均有提高。     

配合物Zn(Him)2(OAc)2的室温固相合成及表征

乙酸锌与咪唑 (Him)通过室温固相反应一步合成配合物Zn(Him) 2 (OAc) 2 ,反应不需溶剂 ,2 0min即可完成 ,产率达 96% ,并用元素分析、红外光谱、热重分析、X -射线粉末衍射和X -射线单晶衍射对产物进行了表征。     

黑液中的多糖对合成本素胺乳化剂的影响

直接以浓缩黑液为原料，通过环氧氯丙烷引入季铵基团制取阳离子型木素胺乳化剂。对产品和原料黑液做了剖析，证明黑液中的非本素有机物发生了胺化反应．应用试验证明这部分胺化产物具有助乳化和稳定乳液的作用。     

羟胺-环己酮法肟化反应效率的影响因素及改进措施

介绍了羟胺-环己酮法中环己酮肟化反应的原理及工艺流程,讨论了反应温度、环己酮进料的分布、缓冲溶液的pH值、脉冲速度等因素对肟化反应效率的影响,针对各个影响因素提出了改进肟化反应条件的措施并应用于生产实践,提高了肟化反应效率。     

常温脱氯剂与HCl气体反应动力学的研究

在固定床反应器中研究了自制的铁系常温脱氯剂与HCl气体的反应动力学,导出了计算脱氯剂氯容的动力学方程q=0.309[(exp(0.036t))/(exp(0.036t)+exp(61.9Z)-1)]×100%.根据该方程,可以计算各个时刻、床层不同深度处脱氯剂的氯容,从而判断脱氯剂的性能及其使用寿命.     

MAXIMIZING SELECTIVITY OF LIQUID-LIQUID REACTION SYSTEMS. CONTROL OF THE DISPERSION PROCESS

Currently available information on droplet coalescence and break-up rates in turbulent flows in mixing vessels can be used to control drop sizes in dispersed phase equipment. The effect of drop size distributions on the selectivity and productivity in multi-reaction systems is examined in this paper.

The reaction system features the primary desired product (C) as resulting from reaction (in the bulk phase) between a reactant (A) in the drop phase and a second reactant (B) in the bulk phase. An adverse reaction is also envisaged which consumes (C) by further reaction with (B) to form a waste product. While small drops promote conversion because of large interfacial area, larger drops promote selectivity because of the facility of the product to re-enter the drop phase avoiding further reaction (to form waste) in the bulk phase. The effect of the bivariate distribution of drop size and reactant (A) concentration in the feed to a continuous stirred tank reactor on the selectivity and productivity of (C) is investigated within the framework of film theory while neglecting drop dynamics such as coalescence and break-up.

The results show the selectivity can be substantially improved by controlling drop size and distribution of the reactants among the differently sized droplets. Contrary to conventional wisdom which emphasizes creation of interfacial area by promoting very small droplets, it emerges that optimal distributions of drop size and reactant concentration which maximize productivity of the desired product exist. The practical implications are discussed.     

Direct ethoxylation of fatty methyl ester over Al-Mg composite oxide catalyst

For the purpose of estimating the reaction mechanism of the direct ethoxylation of a fatty ester in the presence of an Al-Mg composite oxide catalyst, a labeled fatty methyl ester C₁₁H₂₃CO¹⁸OCH₃ containing ¹⁸O isotope was synthesized and directly ethoxylated. The product was evaluated by gas chromatography-mass spectrometry (GC-MS). The GC-MS spectra showed that the ¹⁸O isotope label was present only in the methoxy group at the molecular end of the ethoxylated fatty methyl ester. This supports the reaction mechanism of coordination anionic polymerization where the bond between the acyl and methoxy groups of the fatty methyl ester molecule was broken, caused by the bifunctional effect of the acid-base active sites; an intermediate chemisorption species was formed; and then ethylene oxide was addition-polymerized sequentially, in parallel.