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Preparation of supported asymmetric carbon molecular sieve membranes

机译:负载型不对称碳分子筛膜的制备

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Asymmetric carbon membranes were made by casting a solution of 13 wt% polyamic acid in N-methylpyrrolydone (NMP) upon a macroporous carbon support. The polymeric solution was coagulated in a bath of isopropyr alcohol and dried at room temperature and at 150 degrees C in air. The resulting polymer was heat treated under vacuum involving two steps: (1) imidization at 380 degrees C during 1 h(heating rate: 1 degrees C/min) and (ii) carbonization at 550 degrees C for 1 h (heating rate: 0.5 degrees C/min). The carbon membrane obtained in only one casting step shows an asymmetric structure formed by a dense skin layer with a thickness of around 1 mu m and a porous substrate (approximate to 6 mu m thickness) of the same material. The gas permeation results indicate that the gas transport through the membrane occurs according to an activated mechanism (molecular sieving). The selectivity and permeation rate measured at 25 degrees C for the O-2/N-2, He/N-2, and CO2/CH4 systems were respectively: alpha(O-2/N-2)=5.3, P(O-2)= 1.14x 10(-9) mol/m(2) s Pa; alpha(He/N-2)=26.5, P(He)=5.7 x 10(-9) mol/m(2) s Pa; alpha(CO2/CH4)=37.3, P(CO2)=4.0x 10(-9) mol/m(2) s Pa. (C) 1998 Elsevier Science B.V. [References: 15]
机译:将13 wt%聚酰胺酸的N-甲基吡咯烷酮(NMP)溶液浇铸在大孔碳载体上,制备不对称碳膜。将聚合物溶液在异丙嘧醇浴中凝固,并在室温和150°C空气中干燥。所得聚合物在真空下进行热处理,包括两个步骤:(1)在380°C下亚胺化1小时(加热速率:1°C/min)和(ii)在550°C下碳化1小时(加热速率:0.5°C/min)。仅通过一个铸造步骤获得的碳膜显示出由厚度约为1μm的致密表皮层和相同材料的多孔基板(厚度约为6μm)形成的不对称结构。气体渗透结果表明,气体通过膜的传输是根据激活的机制(分子筛分)发生的。在25°C下,O-2/N-2、He/N-2和CO2/CH4体系的选择性和渗透率分别为:α(O-2/N-2)=5.3,P(O-2)=1.14x 10(-9) mol/m(2) s Pa;α(He/N-2)=26.5, P(He)=5.7 x 10(-9) mol/m(2) s Pa;alpha(CO2/CH4)=37.3, P(CO2)=4.0x 10(-9) mol/m(2) s Pa. (C) 1998 Elsevier Science B.V. [参考文献: 15]

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