完全液相法与溶胶-凝胶法制备Cu-Zn-Al双功能催化剂对浆态床一步法合成二甲醚的催化性能比较

采用完全液相法和溶胶-凝胶法分别制备了组成完全相同的Cu-Zn-Al双功能催化剂,用XRD、氮气吸附-脱附实验和XPS等手段对催化剂的性质进行表征,考察了催化剂对浆态床一步法合成二甲醚反应的催化性能.结果表明,两种方法制备的Cu基催化剂中Cu组分的物相和表面Cu含量明显不同,而催化剂的织构性质基本相同.完全液相法制备的...     

一种新型光电催化反应器的研制及甲酸的光电催化深度氧化

 研制出一种新型的悬浮态光电催化反应器，并以甲酸为研究对象，对该光电反应器进行了光电流增强和COD脱除的表征．研究了光催化、电催化氧化及光电协同催化体系降解甲酸的电压－电流曲线．数据表明，在相同的电压下，光电协同催化体系的电流远高于电化学氧化体系的电流与光催化体系中光电流之和．同时，还研究了一系列物理化学因素如外加电压、光催化剂浓度和空气流量等对光电催化反应的影响．实验结果表明，自行研制的新型悬浮态光电催化反应器具有良好的协同效应，且所需光催化剂的最佳浓度远低于其他同类光电催化反应器的最佳浓度．在该光电催化反应器中，压缩空气可有效地增强传质效应和悬浮态中光激发的TiO2颗粒在电极表面的碰撞几率，从而使得外电场可有效地捕获光生电子．     

闪蒸分离的低温液相甲醇合成的研究

为了强化传质和反应操作,同时实现反应产物与浆液的分离,使用CuCr/CH3ONa催化体系,在鼓泡浆液反应器(BCSR)、闪蒸塔(FC)和浆液循环泵组成的反应系统（BCSR FC）中考察了低温甲醇合成的反应性能。初始浆液由铜铬催化剂、甲醇钠溶液、乳化剂OP 10和液相介质二甲苯组成。在BCSR:4.2MPa～4.6MPa,110℃～120℃(反应段)100℃～110℃(扩大段),入口气速0.35cm/s～0.40cm/s;FC:0.25MPa～0.40MPa,80℃～90℃,浆液循环量50L/h下, 100h实验期间,合成气转化率、CO转化率和H2转化率分别从最高的71.0％、79.1％和67.5％降到17.8％、35.0%和12.1%。催化体系失活的主要原因是CH3ONa 和MeF反应生成甲酸钠。液体产物由DME 1.23%、甲醇79.52%、MeF 19.25%组成。甲醇＋MeF的选择性大于98％。以系统中催化剂为基准,液体产物的产率则为0.166g/gcat·h; BCSR中CuCr催化剂的液体产物的产率为0.336g/gcat·h。     

磁性催化剂与磁稳定床反应器

将非晶态Ni加氢性能和磁性与磁稳定床反应器相结合,工业应用于已内酰胺加氢精制过程,实现了加氢反应过程的强化。在此基础上制备了系列磁性催化剂,包括金属氧化物催化剂、负载型双金属催化剂和强酸性磁性树脂催化剂等。上述磁性催化剂与磁稳定床反应器相结合,用于CO加氢、乙炔选择性加氢、烯烃叠合和醚化等反应,同样表现出反应过程强化的特点。本文结合我们自己的研究工作,对近年来磁稳定床反应器与磁性催化剂的研究进展进行了评述,并展望了未来磁性催化剂与磁稳定床反应器的发展趋势。     

反应-扩散斑图反应器*

本文综述了在反应-扩散斑图研究中反应器的进展情况。直到20世纪80年代,人们主要在培养皿中研究封闭体系的化学波。为了研究体系在远离平衡态条件下的复杂时空动力学行为,近二十年来人们设计出许多新颖的空间开放反应器(continuously fed unstirred reactor,CFUR)如单边进料反应器(one side fed reactor,OSFR)、双边进料反应器、圆盘形凝胶、圆环形凝胶反应器以及Couette反应器等。反应介质主要为各种凝胶、微孔膜、离子交换树脂以及中孔玻璃。空间开放反应器的设计和发展极大地促进了化学斑图动力学的发展。同时讨论了反应-扩散斑图反应器结构设计遇到的困难如气泡和三维效应,并且对反应器设计与斑图研究未来发展方向进行了探讨。     

安全壳中钢衬壳热屈曲问题理论与实验研究（Ⅱ）—实验部分

钢衬壳热屈曲问题是核工程安全壳设计中的主要问题,但实验研究方面的文章发表得不多。文中以２００兆瓦核电站安全壳中钢宙为研究对象,采用局部１：１模型,测得了钢衬壳热屈曲温度和应变载荷,给出了钢衬壳屈曲和初始后屈曲过程中挠度和温度关系。     

移动床热煤气脱硫气固反应过程模拟 Ⅰ错流移动床反应器模型建立

热煤气脱硫是ＩＧＣＣ等高效洁净煤联合循环发电过程的关键技术,本文采用具有净化（脱硫及除尘）一体化潜力并可实现过程连续操作的错流移动床为热煤气脱硫反应器,通过对其反应过程的分析作出合理假设,建立了描述单颗粒脱硫反应及反应器行为的模型方程,并进行了初步的数值模拟计算,结果表明本模型的计算结果可较好地解释前人的实验工作,可对错流移动床反应器的行为作出合理预测     

Influence of Operating Conditions on BaSO4 Crystal Size and Morphology in a Continuous Couette Precipitator

Precipitation of a sparingly soluble salt in the annular gap of a continuous Couette reactor with two unpremixed feeds has been experimentally investigated. Barium chloride and sodium sulphate in stoichiometric ratio are fed at different flow rate in the lower part of the reactor; different feeding modes have been considered. The dependence of precipitation yield, mean crystal size and particle size distribution on rotation speed, axial flow rate and initial supersaturation ratio has been studied. Depending on the operating conditions crystals with different morphologies have been obtained, varying from dentritic tabular crystals to complex pyramidal ones and from single crystals to aggregates. This revised version was published online in August 2006 with corrections to the Cover Date.     

Ethanol production from corn starch in a fluidized-bed bioreactor

The production of ethanol from industrial dry-milled corn starch was studied in a laboratory-scale fluidized-bed bioreactor using immobilized biocatalysts. Saccharification and fermentation were carried out either simultaneously or separately. Simultaneous saccharification and fermentation (SSF) experiments were performed using small, uniform κ-carrageenan beads (1.5–2.5 mm in diameter) of co-immobilized glucoamylase and Zymomonas mobilis. Dextrin feeds obtained by the hydrolysis of 15% drymilled corn starch were pumped through the bioreactor at residence times of 1.5–4h. Single-pass conversion of dextrins ranged from 54–89%, and ethanol concentrations of 23–36 g/L were obtained at volumetric productivities of 9–15 g/L-h. Very low levels of glucose were observed in the reactor, indicating that saccharification was the rate-limiting step. In separate hydrolysis and fermentation (SHF) experiments, dextrin feed solutions of 150–160 g/L were first pumped through an immobilized-glucoamylase packed column. At 55°C and a residence time of 1 h, greater than 95% conversion was obtained, giving product streams of 162–172 g glucose/L. These streams were then pumped through the fluidized-bed bioreactor containing immobilized Z. mobilis. At a residence time of 2 h, 94% conversion and ethanol concentration of 70 g/L were achieved, resulting in an overall process productivity of 23 g/L-h. Atresidence times of 1.5 and 1 h, conversions of 75 and 76%, ethanol concentrations of 49 and 47 g/L, and overall process productivities of 19 and 25 g/L-h, respectively, were achieved.     

In-Situ Monitoring of Emulsion Polymerisations of MMA and Styrene Using Conductimetry and Calorimetry

In the present work, conductimetry is applied for on-line evaluation of anionic surfactant dynamics during emulsion polymerisation of methyl methacrylate and styrene and for on-line estimation of particle size and number. Reactor and jacket temperatures are used to perform energy balance computations on-line and to provide on-line evaluation of monomer conversion. The parameters of a previously proposed model are re-estimated in order to describe the conductivity signal during methyl methacrylate runs. Some important issues regarding the effects of the surfactant micelles over the conductivity signal are addressed. Finally, the model is inverted and combined with conversion and reactor temperature measurements, providing good predictions of the number of polymer particles in the latex, without needing of on-line measurements of particle size.