F2.4微孔膜的制备及在膜蒸馏过程中应用的初步研究

采用相转化法制备了F2 4的疏水微孔膜 ,并对F2 4和PVDF微孔膜的机械性能以及疏水性等方面进行了对比 .结果表明 ,F2 4微孔膜在拉伸时的应变以及断裂伸长率约为PVDF微孔膜的 6～ 9倍 ;其接触角 (77 4°)也大于PVDF膜的接触角 (6 6 7°) .尽管膜蒸馏的数据显示F2 4微孔膜的蒸馏通量尚不及PVDF膜 ,但通过调节各项制膜参数 ,F2 4可能具有良好的应用前景     

超声监测技术在膜分离过程中的应用研究

在膜分离过程中，膜通量总是随运行时间而下降．为了区分膜污染与浓差极化或者可能的膜形变对通量的影响，和选择适宜的清洗过程，对一种只敏感于膜表面状况的超声测量方法进行了广泛研究．通过平板膜(包括微滤膜、超滤膜和反渗透膜)以及卷式反渗透膜过程的应用实例，说明了这种实时、在线的超声时域反射法即Ultrasonic Time-Domain Reflectometry (UTDR)可以利用它的反射波的振幅和回声抵达超声传感器的时间来监测浓差极化、膜污染(例如CaSO4污染)与清洗过程，也可以用来测量膜的压紧度和污染层厚度．超声测量与传统膜性能测量结果有良好的关联，并具有区域性测量的特性．为了实用化目的，新近的研究进展也作了介绍．     

建筑艺术--膜结构建筑

结合具体工程实例 ,介绍了膜结构建筑 ,从其类型、膜材料的种类、膜结构建筑的特点等方面进行了论述 ,展望了2 1世纪膜结构建筑的发展。     

Separation of weak and strong acids by electro-electrodialysis—Experiment and theory

The experimental results of the separation of acetic acid (HA) from the sulfuric acid by the electro-electrodialysis (EED) method and the modeling of process have been presented. The Neosepta membranes CMX and ACM have been used. It has been found that the efficiency of retention of HA is high (>0.9) when the process is conducted below the limiting current density with respect to HSO₄⁻ or SO₄²⁻ anions. The observed current efficiency of the H₂SO₄ removal was rather low (CE_S = ca. 0.7, when the initial concentration of H₂SO₄ in the mixture was 1 or 2 M) which was caused by the nonideal selectivity of the anion-exchange membrane. The experimental results have been described by the model based on the extended Nernst-Planck equation and the Donnan equilibrium. Since the efficiency of the process depended mainly on the selectivity of anion-exchange membrane (ACM), the concentration of fixed charges of that membrane, , and the ratio of volume fraction of pores to their squared tortuosity, V_p/θ², have been chosen as the main fitting parameters. It has been found that the fitting of the EED data depends mainly on , whereas in the modeling of diffusion experiment (or an EED experiment conducted at low current density) both parameters are important. The best fit has been obtained for , i.e. ca. one order smaller than that determined experimentally. The obtained optimal value of V_p/θ², equal to 0.013, is consistent with those previously obtained for other Neosepta anion-exchange membrane.     

膜控晶体生长及纳米微粒的形成

膜控晶体生长不同于一般在溶液中的沉淀与结晶，由膜形成的有机界面具有空间定位和空间约束、定域化学控制及成核过程和晶体生长的立体化学专一的特性，使得晶体的结构、形状和尺寸上得到控制，并具有良好的重现性，由此可获得具有光、电以及磁特性的纳米功能材料。研究膜控晶体生长不仅可以模拟生物体系内的生物矿化作用，而且对于材料科学也有着特别重要的意义和应用前景。     

Effects of growth with ethanol on fermentation and membrane fluidity of Saccharomyces cerevisiae

Saccharomyces cerevisiae HSc was grown with ethanol at concentrations up to 10% (v/v). The immediate effects of additions of externally added ethanol on CO₂ production and O₂ consumption of washed organisms were studied by stopped-flow membrane inlet quadrupole mass spectrometry. Fermentative activities of organisms grown with ethanol (0–5% v/v) showed similar sensitivities to inhibition by ethanol, whereas those grown with 10% (v/v) ethanol had become protected and were markedly less sensitive. The fluidity of subcellular membrane fractions was measured by determination of the temperature dependence of the rotational order parameter of the spin label 5-doxyl stearic acid (free radical) by electron spin resonance. Mitochondria prepared from yeasts grown with 0, 7 and 9% (v/v) ethanol showed similar overall fluidity, although differences in temperature-dependent behaviour indicate altered lipid composition or lateral phase separations. On the other hand the microsomal fraction from organisms grown with 9% ethanol showed a remarkable increase in fluidity. These data suggest that the protective effects of growth with ethanol near the limit of tolerance on fermentative activities may arise from altered plasma membrane fluidity properties.     

锥形阀压电薄膜泵的初步研究

提出一种适应高频工作状态的压电薄膜泵结构，实步分析了所采用的锥形阀的工作原理与作用，设计了试验泵结构，加工了样机，通过试验证明了锥形阀的有效性，为进一步的研究打下了基础。     

New strategies for separations through reactions

Separations through reactions can provide reliable and economically viable alternatives to established methods of separation, particularly for close boiling substances. New strategies in ‘Dissociation Extraction’ and ‘Dissociation Extractive Crystallization’ for separation of close boiling acidic/basic mixtures have been highlighted. Separations with aqueous solutions of hydrotrope and aqueous micellar solutions have been brought out. Separations by membranes with facilitated transport is potentially attractive. This paper is dedicated to Dr L K Doraiswamy on his sixtieth birthday.     

Coupling of reaction and separation at the microscopic level: esterification processes in a H-ZSM-5 membrane reactor

A catalytically active zeolite membrane has been used to displace equilibrium by selective water permeation during ethanol esterification. Unlike previous works in which water separation was carried out by zeolitic membranes that did not take part in the reaction, the H-ZSM-5 membrane used in this work had sufficient catalytic activity to carry out the esterification of ethanol with acetic acid, and at the same time was selective for water permeation. As a consequence, the reaction and separation functions could be coupled very efficiently, and the conversion obtained at the same feed rate and catalyst loading was greater than in conventional fixed bed reactors, or in reactors where the zeolite membrane was kept separated from the catalyst.     

膜催化氧化正丁烷制顺酐

以多孔玻璃管为基体，制备４种用于正丁烷氧化制顺酐的膜反应器。在一定的操作条件下，考察了固定床反应器与这４种膜反应器在正丁烷氧化制顺酐中的反应性能并加以比较，发现ＹＳＺ膜反应器可获得高于固定床反应器的选择性和收率。