渗透汽化型酯化膜反应器研究聚合物／无机固体酸管式复合膜？…

设计了渗透汽化型管式膜反应器,以乙酸丁酯合成反应为探针,考察了Ｚｒ（ＩＶ）／ＰＶＡ,Ｚｒ（ＩＶ）－ＰＶＡ／ＰＶＡ两类聚合物担载无机固体酸管式复合膜的膜催化反尖性能。探讨了功能膜的组成,结构,反应条件等对膜反应和分离性能的影响以及同步膜分离过程对反应转化的促进作用。实验结果表明,膜催化酯化反应过程主要是依赖与料液接触侧膜表面层的催化活性,膜的催化活性是影响反应速率,特别是初期反应转化速率的主要因素,     

Zr（IV）／PVA功能膜的膜催化酯化反应研究

在催化与渗透汽化分离技术相偶合的渗透汽化型膜反应器中，研究了羧酸酯的液相合成反应。实验中制备了两类具有强酸催化活性的Ｚｒ（Ⅳ）／ＰＶＡ（聚乙烯醇）功能膜，采用管式膜方式，以乙酸正丁酯的合成反应为探针，对这类新型的催化反应技术在催化活性、分离性能以及分离对反应转化的影响等方面进行了探索性研究。从得到的结果看，膜催化酯化反应过程的反应条件和缓，转化率可达到９８％，反应的选择性为１００％。     

渗透汽化型酯化膜反应器研究——PVA/PSSA共混聚合物管式复合膜的膜反应性能

聚合物共混是制备具有预定性能的功能膜材料的有效方法．报道了以惰性素烧陶瓷管为支撑体的ＰＶＡ／ＰＳＳＡ共混聚合物管式复合膜的制备及其在渗透汽化型酯化膜反应器中不同实验条件下的膜催化反应性能．探讨了共混膜的组成,反应温度等对膜反应和分离性能的影响以及同步膜分离过程对反应转化率的促进作用．交联ＰＶＡ／ＰＳＳＡ管式复合膜具有良好的催化和分离性能．     

Zr（Ⅳ）／PVA功能膜的膜催化酯化反应研究

在催化与渗透汽化分离技术相偶合的渗透汽化型膜反应器中，研究了羧酸酯的液相合成反应．实验中制备了两类具有强酸催化活性的ｚｒ（Ⅳ）／ＰＶＡ（聚乙烯醇）功能膜，采用管式膜方式，以乙酸正丁酯的合成反应为探针，对这类新型的催化反应技术在催化活性、分离性能以及分离对反应转化的影响等方面进行了探索性研究。从得到的结果看，膜催化酯化反应过程的反应条件和缓，转化率可达到９８％，反应的选择性为１００％．     

过氯乙烯膜渗透汽化性能的研究

将过氯乙烯（ＣＰＶＣ）作为渗透汽化膜材料，用于分离乙醇／水溶液，研究了膜对水和乙醇的吸附溶解性能，对乙醇／水溶液的分离性能，分离温度对膜分离性能的影响。发现过氯乙烯膜优先透水，对乙醇／水溶液选择性高而透量较小。膜的稳定性较好。     

中空纤维催化膜反应器中环戊二烯的选择加氢反应

将聚乙烯吡咯烷酮（ＰＶＰ）负载钯催化剂（ＰＶＰ－Ｐｄ）镶嵌到三种醋酸纤维（ＣＡ）中空膜（ＣＡ－Ｉ，ＣＡ－Ⅱ，ＣＡ－Ⅲ）内制各中空纤维催化膜，并进一步制成催化膜反应器，在４０℃和０．１ＭＰａ的反应条件下，在催化膜反应器中进行了环戊二烯的选择加氢反应，考察了具有不同氢气渗透率的醋酸纤维丝组成的三种膜反应器对反应的转化率及选择性的影响，并在此基础上考察了各种反应参数对反应的影响，ＣＡ中空纤维催化膜对环戊     

PVA／PEG共混渗透蒸发膜的盐水分离机理研究

以聚乙烯醇（ＰＶＡ）和聚乙二醇（ＰＥＧ）共混,甲醛交联制备亲水性高分子膜,用于渗适蒸发过程进行海水脱盐。ＰＥＧ的引入使盐－水分离成为可能, 到钠的引入使膜的分离通量明显提高。通过溶用蔗、ＰＥＧ水溶液的粘度和膜形态分析等方法对ＰＶＡ－ＰＥＧ体系的高分子网络结构和膜中相分离作了研究,发现了膜结构与渗透蒸发脱盐性能的基本关系。影响膜分离的因素除了化学亲合性之外,主要是膜的溶胀性和微相分离程度。ＰＥＧ的作     

聚丙烯腈原液膜的制备和性能

以溶液聚合的聚丙烯腈原液为铸模液，研究了溶液铸腊法工艺参数：铸膜液温度、凝胶水温度、铸膜液浓度等对膜性能的影响。结果表明，不存在蒸发时间的影响以及不调整原液的组分和浓度是聚俩烯腈原液于其它膜制作技术的显著特点。调节有关制膜工艺参数即可获得特定用途的超滤分离膜。在具有三层结构、平均孔径为５ｎｍ的聚丙烯腈原液干膜上复合了聚乙烯醇（ＰＶＡ）的ＰＶＡ／ＰＡＮ复合膜，分离醇水溶液的渗透汽化（ＰＶ）性能优良。     

一种新的适合低pH范围的中性载体PVC膜电极的研究

设计并合成了Ｎ－十八烷基水杨醛亚胺（ＯＤＳＡＩ）,Ｎ－十八烷基苯甲醛亚胺（ＯＤＢＡＩ）两种新的亚胺化合物,并以此为中性载体,制成了ＰＶＣ膜ＰＨ电极。此电极在ＰＨ０．６－８．５的范围内,对氢离子呈现很的能斯响应,电极斜率为５２ｍＶ／ｐＨ。     

再生纤维素／聚乙烯醇共混膜的研究

由纤维素铜氨溶液与不同体积比（１－１０％）的聚乙烯醇（ＰＶＡ）水溶液共混制备了一系列再生纤维素共混膜．扫描电镜结果表明ＰＶＡ含量大于８％时，该共混膜产生明显相分离．当ＰＶＡ低于５％时，共混膜相容性较好．膜的结晶度，抗张强度，直角撕裂强度，断裂伸长及耐热性均优于单独用钢氨液制备的再生纤维素膜．此外，用流动速率法和超滤法测定了膜的孔径，渗透性及纯水通量，结果表明共混膜的孔性没有明显变化．本文得出：再生纤维素与５％ＰＶＡ共混能改善力学性能，并且能保持其生物降解性．     

PEG-grafted PVA Membrane and Its Blood Compatibility

Preparation and blood compatibility of different shape polyvinyl alcohol(PVA) membrane were investigated. Firstly, the tabular and tubular[polytetrafluoroethylene(PTFE) capillary as supporter] PVA membranes were prepared; then, methoxy polyethylene glycol(mPEG) was grafted onto the surface of the PVA membranes. The effects of the shape, structure and properties of the membrane surface on blood compatibility were studied in detail. The experiment results show that mPEG modified PVA membranes, especially mPEG modified tubular membrane, could availably repel the adhesion of the platelets. In addition, the anticoagulant mechanism of mPEG with a steric repulsion effectiveness was confirmed further via different grafting methods.     

Pervaporation separation of water-acetic acid mixtures through poly(vinyl alcohol) membranes crosslinked with glutaraldehyde

Poly(vinyl alcohol) (PVA) membranes crosslinked with glutaraldehyde (GA) were prepared by a solution method for the pervaporation separation of acetic acid-water mixtures. In the solution method, dry PVA films were crosslinked by immersion for 2 days at 40°C in reaction solutions which contained different contents of GA, acetone and a catalyst, HCl. In order to fabricate the crosslinked PVA membranes which were stable in aqueous solutions, acetone was used as reaction medium in stead of aqueous inorganic salt solutions which have been commonly used in reaction solution for PVA crosslinking reaction. The crosslinking reaction between the hydroxyl group of PVA and the aldehyde group of GA was characterized by IR spectroscopy. Swelling measurements were carried out in both water and acetic acid to investigate the swelling behavior of the membranes. The swelling behaviour of a membrane fabricated at different GA content in a reaction solution was dependent on crosslinking density and chemical functional groups created as a result of the reaction between PVA and GA, such as the acetal group, ether linkage and unreacted pendent aldehydes in PVA. The pervaporation separation of acetic acid-water mixtures was performed over a range of 70–90 wt% acetic acid in the feed at temperatures varying from 35 to 50°C to examine the separation performances of the PVA membranes. Permeation behaviour through the membranes was analyzed by using pervaporation activation energies which had been calculated from the Arrhenius plots of permeation rates.     

中空纤维Au-CeZr/FAU催化膜的制备及在富氢气氛CO选择性氧化反应中的应用

采用浸渍法制备了一系列不同Ce/Zr掺杂比例的FAU分子筛膜, 并进一步负载纳米金, 制备了Au-CeZr/FAU催化膜. 对催化膜的微观形貌及结构进行了表征, 并对其在富氢气氛中催化CO优先氧化性能进行了研究. H₂-TPR结果表明, Ce/Zr掺杂比为1∶1时制得的催化膜Au-Ce₁Zr₁/FAU具有最好的被还原能力, 更有利于Au的分散与还原; O₂-TPD结果表明, 该样品的氧物种比其它样品上的氧物种活性更高. 更好的被还原性能和更高的氧物种活性使得制备的Au-Ce₁Zr₁/FAU催化膜性能最佳, 在60 ℃时CO转化率与O₂选择性可以同时达到100%, 并且在经过10次热循环测试后仍然可以保持稳定的催化性能.     

耗散粒子动力学模拟Nafion膜和PVA/Nafion共混膜的介观结构

采用耗散粒子动力学模拟方法研究了水化Nafion膜和水化聚乙烯醇(PVA)/Nafion共混膜的微结构.模拟结果表明水化Nafion膜和水化PVA/Nafion共混膜均能形成相分离的微结构.在水化Nafion膜中,水与磺酸根混合形成管状的水团簇.随着膜内水含量增多,管状水团簇的尺寸逐渐变大并在膜内形成连续的水通道.在水化PVA/Nafion共混膜中,PVA、水、磺酸根混合形成亲水性区域.共混膜中PVA的质量分数和水含量共同影响膜的微结构.当膜中PVA质量分数较低时,PVA主要分布在Nafion的磺酸根基团周围;PVA质量分数升高后,PVA会在膜内单独成一相.当膜中的水含量相对较低时,水分子会溶解于PVA中,此时膜内不存在单独的水团簇;膜中的水含量增多后,膜内会形成接近于球形的水团簇.本文工作可为直接甲醇燃料电池用的PVA改性Nafion膜的开发提供参考.     

Nanofibrous Tubular Membrane for Blood Hemodialysis

As the most important components of a hemodialysis device, nanofibrous membranes enjoy high interconnected porosity and specific surface area as well as excellect permeability. In this study, a tubular nanofibrous membrane of polysulfone nanofibers was produced via electrospinning method to remove urea and creatinine from urine and blood serums of dialysis patients. Nanofibrous membranes were electrospun at a concentration of 11.5 wt% of polysulfone (PS) and dimethylformamide (DMF)/tetrahydrofuran (THF) with a ratio of 70/30. The effects of the rotational speed of collectors, electrospinning duration, and inner diameter of the tubular nanofibrous membrane on the urea and creatinine removal efficiency of the tubular membrane were investigated through the hemodialysis simulation experiments. It was found that the tubular membrane with an inner diameter of 3 mm elecrospun at shorter duration with lower collecting speed had the highest urea and creatinine removal efficiency. The hemodialysis simulation experiment showed that the urea and creatinine removal efficiency of the tubular membrane with a diameter of 3 mm were 90.4 and 100%, respectively. Also, three patients’ blood serums were tested with the nanofibrous membrane. The results showed that the creatinine and urea removal rates were 93.2 and 90.3%, respectively.     

Ti(IV)-based catalytic membranes for efficient and selective oxidation of secondary amines

The incorporation of homogenous Ti(IV)/trialkanolamine catalyst in polymeric membranes provided new polymeric catalytic Ti(IV)-based membranes, stable and efficient as heterogeneous catalysts for chemoselective oxidations of secondary amines to nitrones by alkyl hydroperoxides. Polyvinylidene fluoride (PVDF)-based catalytic membranes gave the best results affording products in short reaction times, high yields and selectivity using as little as 1% of catalyst, comparable with the performances of the corresponding homogeneous system. PVDF-Ti membrane could be recycled up to five runs with no loss of activity.     

Hydrogenolysis and Hydroisomerization of Neopentane on Titanium and Zirconium Hydrides Stabilized on the Surface of SiO2: A Theoretical Study by Density Functional Theory

The model reactions of neopentane hydrogenolysis and hydroisomerization on transition metal hydrides (≡ Si?O)₃M^IVH (1), (=eqSi?O)₂MIVH² (2), and (≡Si?O)₂M^IIIH (3) (M = Zr, Ti) immobilized on the surface of silica were studied by density functional theory. It was shown that the hydrogenolysis of neopentane could occur on all the three types of metal hydrides, the catalytic activity of reaction centers increasing along the series M(IV) monohydrides 1 < M(IV) dihydrides 2 < M(III) hydrides 3. At the same time, the isomerization of the hydrocarbon skeleton of neopentane observed experimentally on titanium-based systems could only be explained by the participation of Ti(III) hydrides.     

Analysis of mixtures of hafnium and zirconium by the methylthymol blue-hydrogen peroxide method

The reaction of hydrogen peroxide with the zirconium(IV) and hafnium(IV) Methylthymol Blue complexes (MeMTB) has been investigated. The conditional stability constants of the Zr(IV) and Hf(IV) complexes with hydrogen peroxide [K'(Me(H(2)O(2)))] were determined spectrophotometrically. The K'(Me(H(2)O(2))) values found, which depend on the acidity, are 3.91 x 10(2) 3.24 x 10(2), 2.63 x 10(2) at [HCl] = 0.2, 0.3, 1.0M respectively for Me = Zr(IV) and 0.828, 0.523, 0.319 for Me = Hf(IV). The ratios of the conditional stability constants, K'(Me(H(2)O(2)))/ K'(MeMTB), are: 5.52 x 10(-4), 5.79 x 10(-4), 8.23 x 10(-4) for Me = Zr(IV) and 2.08 x 10(-6), 2.74 x 10(-6), 1.48 x 10 (-5) for Me = Hf(IV) at the three acidities. The maximum of the ratio of the relative conditional stability constants is obtained in 0.2M hydrochloric acid. The conditions which should be complied with for the determination of hafnium in the presence of zirconium are discussed. The results were compared with those obtained by the Xylenol Orange-hydrochloric acid method. They are superior for samples containing less than 20 mole% of hafnium in admixture with zirconium.