support membrane

Preparation of carbon support membrane from petroleum pitch by binderless molding method

石油沥青无粘结剂成型制备炭支撑膜

Optimization of preparation conditions for polyacrylonitrile support membrane using random-arranged experimental designs with aid of computer

用直接实验设计方法优化聚丙烯腈基膜的制备条件

The membrane pollution index FI by PVA solution and the chemical stability are tested . Ideal support membrane is provided for composite membrane .

并测得PVA系列对该膜的污染指数FI及膜的化学稳定性，为复合膜提供了理想的支撑膜。

The effects of preparation conditions such as alkalinity , crystallizing temperature , pretreated method and pore size of the support membrane , on zeolite membrane were also investigated .

最后考察了不同的合成条件包括碱度、晶化温度、多孔载体膜的孔径大小及其予处理方法对分子筛膜的影响。

Scanning electronic microscopy ( SEM ) and atomic force microscopy ( AFM ) showed that there was an active layer with apparent structure of peaks and valleys on the polysulfone support membrane .

扫描电子显微镜（SEM）及原子力显微镜（AFM）可观察到在基膜上复合了一层超薄表层且有明显的峰谷结构。

In this study , we prepared ultrafiltration membrane of polyvinylidene fluoride ( PVDF ) as porous support membrane , and prepared the PVA / PVDF composite membranes on the support membrane by spread method .

本论文还选用聚偏氟乙烯（PVDF）材料，用L-S法制备了聚偏氟乙烯超滤底膜；并以上述PVA交联液为涂层，制备了PVA/PVDF复合膜。

The effects of modification of the internal interface between ultrathin film and support membrane on the performance of composite RO ( reverse osmosis ) membranes have been studied by surface modification of PSF support membranes .

用界面改性的方法研究了多孔支撑层/超薄功能层界面性质对反渗透复合膜性能的影响。

Besides , using PSF-SPES hollow fiber membrane as support membrane and CA aqueous solution as coating solution , CA / PSF-SPES composite membranes were prepared and the performance of the composite membranes was studied . The structure of CA / PSF-SPES ultra-filtration membrane was also discussed .

此外，以PSF-SPES中空纤维为支撑膜，采用醋酸纤维素作为涂层液，研究了CA/PSF-SPES复合超滤膜性能，讨论了CA/PSF-SPES共混中空纤维超滤膜结构。

The SEM analysis of the cross-section of the carbon membrane shows a good combination between the support and membrane .

扫描电镜对炭膜断面微观形态观察表明，膜层与支撑体之间结合良好。

Polyacrylonitrile ( PAN ) support ultrafiltration membrane was successfully prepared by means of phase inversion method , with PAN as raw material , phosphoric acid or polyethylene glycol-600 ( PEG-600 ) as additive and N-methylpyrrolidone ( NMP ) as sol-vent .

以聚丙烯腈为聚合物，磷酸或聚乙二醇-600为添加剂，N-甲基吡咯烷酮为溶剂，采用L-S相转换法制备PAN超滤膜。

The effects of the conditions for making dry membrane and of the different support materials on membrane performance are stated .

介绍了三种膜的机制条件和不同成膜支撑体对膜性能的影响。

Zirconia and Alumina Supported MFI Zeolite Membranes : Effects of Support Materials on Membrane Properties

ZrO2和Al2O3支撑的MFI型沸石分子筛膜：支撑体材料对膜性能的影响

The mean pore sizes of the support , medium membrane and top layer membrane in the asymmetry membrane are 6.6 μ m , 0.6 μ m and 0.1 μ m , respectively .

非对称膜中支撑体、中间层膜和顶层膜的平均孔径分别为6.6μm、0.6μm和0.1μm。

The support is usually ultrafiltration membrane which has a non-symmetrical structure .

一般常用的支撑体为超滤膜，这些膜具有表面平整，中间为指状大孔的非对称结构。

Experimentation of Respiratory Support with Venovenous Extracorporeal Membrane

静脉－静脉体外膜肺氧合支持呼吸的实验研究

Three general approaches may be followed : to be deposited on a porous support , decrease Pd membrane thickness and optimize Pd membrane microstructure .

解决上述瓶颈问题的关键在于：将金属膜沉积在多孔支撑体表面，降低金属膜层厚度，开发新的制膜方法与工艺来改善金属膜微观结构。

This paper presented an extended resistance-in-series model to describe the pervaporation of dilute solution , which encompasses support layer resistance , membrane swelling and component concentration in the vapor mixture .

论文建立了串联阻力模型来描述稀溶液的渗透汽化过程，并将此模型扩展到包括支撑层阻力、膜的溶胀和蒸汽侧组分的浓度。