无机膜反应器对丙烷芳构化历程的影响

根据实验结果，从理论上分析了Ａｌ２Ｏ３无机膜反应器对ＨＺＳＭ－５，０．４％Ｇａ／ＨＺＳＭ－５和０．５％Ｐｔ－０．４％Ｇａ／ＨＺＳＭ－５催化剂上丙烷芳构化反应历程的影响。结果表明，氢气在烷烃活化、环烃形成芳烃和低碳烯烃加氢过程中担当着重要角色，膜反应器通过影响这些步骤，进而影响整个芳构化反应的选择性。     

酸处理Silicalite—I沸石填充硅橡胶渗透蒸发分离膜

研究酸处理Ｓｉｌｉｃａｌｉｔｅ—Ｉ沸石对有机溶剂、水的吸附、脱附性质，酸处理Ｓｉｌｉｃａｌｉｔｅ—Ｉ填充硅橡胶膜对低浓度有机溶剂水溶液的渗透蒸发分离性能以及填充膜的力学性能。实验结果表明，在硅橡胶膜中填充酸处理Ｓｉｌｉｃａｌｉｔｅ—Ｉ沸石能改善膜对有机溶剂－水混合物的分离性能，且分离性能的改善与沸石在膜中的填充量以及硅橡胶的品种有关。另外，沸石的填充也有利于改善膜的力学性能。     

酸处理Silicalite—Ⅰ沸石填充硅橡胶渗透蒸发分离膜

研究酸处理Ｓｌｉｌｉｃａｌｉｔｅ－Ⅰ沸石对有机溶剂、水的吸附、脱附性质，酸处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ填充硅橡胶对低浓度有机溶剂水溶液的渗透蒸发分离性能以及填充膜的力学性能。实验结果表明，在硅橡胶胶膜中填充酸处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ沸石能改善膜对有机溶剂－水混合物的分离性能，且分离性能的改善与沸石在膜中的填充量以及硅橡胶的品种有关。另外，沸石的填充也有利于改善膜的力学性能。     

丙烷在无机膜反应器中的芳构化

研究了在固定床反应器和膜反应器中的丙烷芳构化，考察了ＨＺＳＭ－５担载的Ｇａ和Ｐｔ－Ｇａ催化剂对反应的影响。结果表明，采用无机膜反应器可以提高丙烷芳构化选择性，从而提高芳烃收率达１０％以上。在膜反应器中，低碳烷烃选择性降低，烯烃选择性增强。固定床相比，膜反应器在低温时对芳构化反应的促进作用最为显著，但是随着温度升高，其促进作用减弱。     

沸石分子筛复合膜的制备及其分离水中微量苯酚和苯的性能

探索了如何在过滤陶瓷片上制备Ｓｉｌｉｃａｌｉｔｅ－ｌ和β沸石分子筛复合膜,对它们分离水中微量苯酚和苯的性能进行了考察,并用ＸＲＤ,ＳＥＭ和ＵＶ等测试方法对其物理化学性能和结构进行了表征,结果表明：Ｓｉｌｉｃａｌｉｔｅ－ｌ分子筛膜,两者的平均脱除率分别为６９．９％和５１．５％,通过对Ｓｉｌｉｃａｌｉｔｅ－ｌ沸石分子筛复合膜进行二次合成及高温水蒸气处理,可在很大程度上改善其了性能。     

填充Silicalite－Ⅰ沸石的PDMS橡胶醇－水分离膜

Ｓｉｌｉｃａｌｉｔｅ－Ⅰ沸石经过酸处理或水热处理可完善其晶体结构，提高对乙醇的吸附选择性，由此提高对乙醇－水混合物的分离系数。特别是先经过酸处理再经过水热处理的Ｓｉｌｉｃａｌｉｔｅ－Ⅰ沸石填充聚二甲基硅氧烷橡胶膜（ＰＤＭＳ橡胶膜），乙醇－水的分离系数可达３０左右。     

高硅ZSM－5沸石填充硅橡胶膜的研究（Ⅳ）──沸石粒径和不同品种硅橡胶对乙醇－水混合物渗透蒸发分离性质的影响

研究了粒径为１５μｍ和５μｍ的水热处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ填充ＰＤＭＳ膜以及酸处理Ｓｉｌｉｃａｌｉｔｅ－Ⅰ填充不同品种硅橡胶膜对低浓度乙醇－水混合物的渗透蒸发分离性能的影响。结果表明，沸石粒径的减小，不利于乙醇－水分离系数的提高；不同品种硅橡胶的沸石填充膜对乙醇－水的渗透蒸发分离性能与硅橡胶本身的性质有关。     

高硅ZSM—5沸石填充硅橡胶膜的研究（Ⅳ）：沸石粒径和不同品…

研究了粒径为１５μｍ和５μｍ的水热处理Ｓｉｌｉｃａｌｉｔｅ－Ｉ填充ＰＤＭＳ膜以及酸处理Ｓｉｌｉｃａｌｉｔｅ－Ｉ填充不同品种硅像胶膜对低浓度乙醇－水混合物的渗透发分离性能的影响。结果表明，沸石粒径的减小，不利于乙醇－水分离系数的提高；不同品种硅橡胶有沸石充膜对乙醇－水的渗透蒸发分离性能与硅橡胶本身的性质有关。     

水热处理Silicalite—Ⅰ沸石填充硅橡胶膜Ⅰ对有机溶剂──水混合物的渗透蒸发分离性质

研究水热处理Ｓｉｌｉｃａｌｉｔｅ—Ⅰ沸石对乙醇和水的吸附、脱附性质以及其填充ＰＤＭＳ膜对乙醇、水的渗透蒸发通量和对低浓度有机溶剂一水混合物的渗透蒸发分离性能。实验结果表明，Ｓｉｌｉｃａｌｉｔｅ—Ⅰ沸石经水热处理，其水吸附量大为减少，因此其填充ＰＤＭＳ膜对有机溶剂－水混合物，主要是醇－水混合物的分离系数有显著提高。     

Fe—Silicalite—2催化剂表面CO2加氢反应性能的研究

研究了Ｆｅ／Ｓｉｌｉｃａｌｉｔｅ－２催化剂ＣＯ２加氢低碳烯烃反应性能，利用ＣＯ２－ＴＰＤ，ＣＯ２／Ｈ２－ＴＰＳＲ和ＣＯ／Ｈ２－ＴＰＳＲ表征手段，考察了铁含量及ＭｎＯ助剂对Ｆｅ／Ｓｉｌｉｃａｌｉｔｅ－２催化剂ＣＯ２吸附脱附及加氢反应性能的影响，表明随铁含量增加可提高催化剂对ＣＯ２的吸附能力，有利于提高ＣＯ２加氢反应的转化率。     

荷电膜的膜电位研究进展

膜电位的测定是表征荷电膜的传递现象的重要参数之一。本文简要介绍了膜电位理论基础,包括T. M. S.理论和不可逆热力学理论。分别阐述了关于离子交换膜、双极膜、两性膜以及复合膜的膜电位的最新进展,并提出今后的发展方向。     

透氢钯复合膜的原理、制备及表征

钯及其合金膜由于具有透氢性好和耐高温的特点,除了用作氢气分离和纯化器外,还可以用作脱氢、制氢等反应的反应器,以实现反应和分离的一体化,并提高转化率和选择性。本文综述了钯基复合膜的原理、制备及表征,并重点介绍了本研究组的光催化镀膜工艺。     

高分子纳滤膜的研究及进展

对高分子纳滤膜的发展背景以及国内外在这一领域的研究的研究进展作了详细的介绍。     

透氢钯复合膜的原理、制备及表征

钯及其合金膜由于具有透氢性好和耐高温的特点,除了用作氢气分离和纯化器外,还可以用作脱氢、制氢等反应的反应器,以实现反应和分离的一体化,并提高转化率和选择性。本文综述了钯基复合膜的原理、制备及表征,并重点介绍了本研究组的光催化镀膜工艺。     

纳米复合膜在膜分离领域的研究进展

基于纳米材料的独特性质,将其引入高分子膜所制得的纳米复合滤膜有望解决目前制约膜技术发展的“上限平衡”问题。 本文综述了碳纳米管、石墨烯、SiO2、TiO2、分子筛、ZrO2以及纳米银颗粒等纳米复合膜在膜分离领域的研究进展。 这些纳米材料对于提高复合膜的机械稳定性、亲水性、选择性、渗透性及抗污染能力等有显著的效果。 此外,对纳米复合膜的发展与应用做了展望,也对其研究中存在的问题和解决方法进行了阐述。     

Preparation of Zeolite X Membranes on Porous Ceramic Substrates with Zeolite Seeds

Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50 200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2 0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of γ-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes have zeolitic top-layers with a thickness of 10-25 μm, and zeolite crystals can be intruded into pores of the supports as deeply as 100μm. The experimental results indicate that the precoating of zeolitic seeds on supports is beneficial to crystallization by shortening the synthesis time and improving the membrane strength. The resulting zeolite X membrane shows permselectivity to tri-n-butylamine((C4H9)3N) over perfluro-tributyl-amine ((C4Fg)3N), and a permeance ratio of 57 for ((C4Hg)3N to (C4F9)3N could be reached at 350℃. Permeances of BZ, EB and TIPB through the zeolite membrane were also measured and were found to slightly increase with temperature.     

氯化锂为添加剂制得的疏水聚偏氟乙烯不对称微孔膜的形态结构及其膜蒸馏性能

结合膜的形态结构研究了以 LiCl为添加剂制得的疏水 PVDF膜的膜蒸馏性能。与来用水溶液高分子添加剂制得的PVDF微孔膜相比,膜蒸馏性能有了较大提高,尤其具有更高的截留率。制得的微孔膜的蒸馏通量已接近商品膜的膜蒸馏通量,表明以LiCl为添加剂制得的PVDF疏水微孔膜是一种适用于膜蒸馏的较理想的疏水微孔膜。     

PREPARATION OF SILICALITE-1 AND ZSM-5 ZEOLITE/ CERAMIC COMPOSITE MEMBRANES

ＰＲＥＰＡＲＡＴＩＯＮＯＦＳＩＬＩＣＡＬＩＴＥ┐１ＡＮＤＺＳＭ┐５ＺＥＯＬＩＴＥ／ＣＥＲＡＭＩＣＣＯＭＰＯＳＩＴＥＭＥＭＢＲＡＮＥＳＺｈａｎｇＬｉｘｉｏｎｇ，ＪｉａＭｅｎｇｄｏｎｇ，ＭｉｎＥｎｚｅ（ＲｅｓｅａｒｃｈＩｎｓｔｉｔｕｔｅｏｆＰｅｔｒｏｌｅ...     

Preparation of Zeolite X Membranes on Porous Ceramic Substrates with Zeolite Seeds

Zeolite X membranes were investigated by in-situ hydrothermal synthesis on porous ceramic tubes precoated with zeolite X seeds or precursor amorphous aluminosilicate, and porous α-Al2O3 ceramic tubes with a pore size of 50-200 nm were employed as supports. Zeolite X crystals were synthesized by the classic method and mixed into deionized water as a slurry with a concentration of 0.2-0.5wt%, having a range of crystal sizes from 0.2 to 2μm. Crystal seeds were pressed into the pores near the inner surface of the ceramic tubes, and crystallization took place at 95℃ for 24-96 h. It was also investigated that Boehmite sol added with zeolite X seeds was precoated on ceramic supports to form a layer of r-Al2O3 by heating, and hydrothermal crystallization could then take place to prepare the zeolite membranes on the composite ceramic tubes. The crystal species were characterized by XRD, and the morphology of the supports subjected to crystallization was characterized by SEM. The composite zeolite membranes hav     

Theoretical analysis of the performance of composite membrane consisting of the catalytic and nanofiltration layers

A model of the composite membrane consisting of the catalytic layer (CL) and the nanofiltration layer (NFL) is presented. It has been found that applying NFL on the permeate side of CL it is possible to enhance substantially the conversion of substrate into the product. The best performance is obtained for high retention of substrate and low of product. At higher values of volume flow and/or longer catalytic path the retention degree of product becomes negligible. The presence of NFL enhances the influence of distribution of the reaction rate constant, k, on the conversion ratio. Comparing to k = constant the positive effect is obtained if k increases along the catalytic pore, whereas negative—if k decreases.