多形态ZnO纳米粒子的制备及其紫外—可见光吸收性能研究

选用失水山梨醇单油酸酯／反应物水溶液／环己烷制成微乳液等“微反应器”，在其中控制反应，制备出了具有球形及棒状、不规则片状与球形但呈细胞器状排布的纳米氧化锌。用透射电镜（TEM）、动态激光光微射（DLLS）与X－射线衍射对产物的结构、形态、大小与化学成分进行了表征。系统研究了反应体系的组分、配比、反应温度及分散方法等反应条件对“微反应器”与产物形态、大小的影响。探讨了ZnO纳米粒子的稳定性及其原因。并对ZnO纳米粒子的紫外—可见光吸收性能进行了表征。     

基于烧结微纤多孔结构材料的微反应器中的苯硝化反应

基于烧结微纤结构材料发展了一种集微混合、反应和换热于一体的微反应器,以苯硝化为模型反应考察了该微反应器用于快速、强放热的液-液两相混合反应的效果.烧结微纤材料具有大的空隙率、三维开放孔结构和大的面积与体积比,有利于传质和传热,同时微纤三维网络具有微搅拌器的作用,有利于流体的微米尺度分割和快速混合.因此,苯硝化反应得以在很短的时间内高选择性地进行完全.在一定的操作条件下,苯转化率可以达到91.7%,硝基苯选择性高达99.4%.     

微通道反应器内"就地"合成沸石膜催化层及其性能

采用简单、新颖的沸石粒子引入方法,将NaX沸石晶种引入不锈钢微反应器的微通道内,并用流动法"就地"直接在微通道内通过沸石生长形成NaX沸石膜层,经铯离子交换处理成为CsNaX催化层,用苯甲醛和氰基乙酸乙酯的Knoevenagel缩合反应评价了该催化层的催化性能.结果表明,微通道内形成的沸石膜层连续,均匀,具有良好的催化功能.微反应器内缩合反应的结果明显优于传统反应器.     

Microreactor for the Catalytic Partial Oxidation of Methane

Fixed-bed reactors for the partial oxidation of methane to produce synthetic gas still pose hot-spot problems. An alternative reactor, which is known as the shell-and-tube-typed microreactor, has been developed to resolve these problems. The microreactor consists of a 1 cm outside-diameter, 0.8 cm inside-diameter and 11 cm length tube, and a 1.8 cm inside-diameter shell. The tube is made of dense alumina and the shell is made of quartz. Two different methods dip and spray coating were performed to line the tube side with the LaNixOy catalyst. Combustion and reforming reactions take place simultaneously in this reactor. Methane is oxidized in the tube side to produce flue gases (CO2 and H2O) which flow counter-currently and react with the remaining methane in the shell side to yield synthesis gas. The methane conversion using the higher-loading catalyst spray-coated tube reaches 97% at 700℃, whereas that using the lower-loading catalyst dip-coated tube reaches only 7.78% because of poor adhesion between the catalyst film and the alumina support. The turnover frequencies (TOFs) using the catalyst spray-and dip-coated tubes are 5.75×10-5 and 2.24×10-5 mol/gcat·s, respectively. The catalyst spray-coated at 900℃provides better performance than that at 1250℃because sintering reduces the surface-area. The hydrogen to carbon monoxide ratio produced by the spray-coated catalyst is greater than the stoichiometric ratio, which is caused by carbon deposition through methane cracking or the Boudouard reaction.     

泡沫金属微反应器内富氢重整气中CO选择性甲烷化

在微反应器中,用泡沫金属镍为载体负载4Ni-2Ru/ZrO2双金属催化剂,用于选择性甲烷化去除富氢重整气中的CO。考察了催化剂负载方法、焙烧温度和空速等对CO选择性甲烷化的影响,借助X射线衍射(XRD)、程序升温还原(H2-TPR)等手段对催化剂制备方法与催化性能的关系进行了探讨。结果表明,直接将4Ni-2Ru/ZrO2催化剂涂布在泡沫镍片上,350℃下焙烧,反应温度为260℃,空速为2 000 h-1~6 000 h-1,可将富氢转化气中CO降至30×10-6以下,其中空速为5 000 h-1,可将CO出口浓度降至7×10-6,CO2的转化率低于1.5%。反应温度在260℃~300℃,CO的转化率在99.6%以上,CO出口浓度在50×10-6以下。     

Integration of capillary isoelectric focusing with monolithic immobilized pH gradient,immobilized trypsin microreactor and capillary zone electrophoresis for on‐line protein analysis

An integrated platform consisting of protein separation by CIEF with monolithic immobilized pH gradient (M‐IPG), on‐line digestion by trypsin‐based immobilized enzyme microreactor (trypsin‐IMER), and peptide separation by CZE was established. In such a platform, a tee unit was used not only to connect M‐IPG CIEF column and trypsin‐IMER, but also to supply adjustment buffer to improve the compatibility of protein separation and digestion. Another interface was made by a Teflon tube with a nick to couple IMER and CZE via a short capillary, which was immerged in a centrifuge tube filled with 20 mmol/L glutamic acid, to exchange protein digests buffer and keep electric contact for peptide separation. By such a platform, under the optimal conditions, a mixture of ribonuclease A, myoglobin and BSA was separated into 12 fractions by M‐IPG CIEF, followed by on‐line digestion by trypsin‐IMER and peptide separation by CZE. Many peaks of tryptic peptides, corresponding to different proteins, were observed with high UV signals, indicating the excellent performance of such an integrated system. We hope that the CE‐based on‐line platform developed herein would provide another powerful alternative for an integrated analysis of proteins.     

Modeling of Anionic Polymerization in Flow With Coupled Variations of Concentration,Viscosity, and Diffusivity

This paper explains the reasons behind the very low polydispersity index (PDI) obtained in living anionic polymerizations in microstructured reactors. From the results, it can be explained that a narrow molecular weight distribution can be obtained due to the presence of a highly segregated flow behavior, even in microflow conditions, provided that the mean residence time is high enough. This paper investigates the feasibility of a living anionic polymerization reaction under micro‐fluidic conditions. This is accomplished using a multiphysics model that accounts for the changes in viscosity and diffusivity. These properties descend with the increase in weight of the polymer, and could not be un‐coupled from hydrodynamics and mass transfer. The results of the model are used to understand the reasons behind the very low PDI that can be experimentally obtained in microflow conditions. This leads to the conclusion that the increased viscosity almost “suppresses” the diffusion of the monomer, even at the very short characteristic lengths of a micro‐device. These conditions generate a fully segregated flow that yields an almost monodisperse polymer regardless of the effective residence time distribution encountered in the reactor.

     

Living Anionic Polymerization of tert‐Butyl Acrylate in a Flow Microreactor System and Its Applications to the Synthesis of Block Copolymers

Living anionic polymerization of tert‐butyl acrylate initiated by 1,1‐diphenylhexyllithium is conducted in a flow microreactor system in the presence of lithium chloride. A high degree of control over the molecular weight distribution is achieved under easily accessible conditions, for example at ?20 °C. The subsequent reaction of a reactive polymer chain end with an alkyl methacrylate in an integrated flow micoreactor system leads to the formation of a block copolymer with a narrow molecular weight distribution.