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Morphology and gas permeance of ZSM-5-type zeolite membrane formed on a porous α-alumina support tube

机译:多孔α-氧化铝支撑管上形成的ZSM-5型沸石膜的形貌和透气性

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ZSM-5-type zeolite membranes were synthesized by hydrothermal reaction on the surface of a porous α-alumina support tube of 2.8 mm o.d. and 1.9 mm i.d. The average pore size of the tube was about 150 nm and the void fraction was 0.45. The silicon source was a fine silica powder and the template was a mixture of tetrapropylammoniumhydroxide and bromide. Three zones were observed in the film formed on the support tube. The top zone was a polycrystalline zeolite layer and the inner zone was a layer of α-alumina macropores partially filled with deposits. The intermediate zone was a mixture of alumina particles and deposits. The permeance of the zeolite membranes increased with decreasing thickness of zeolite layer, but permselectivity was not connected with membrane morphology. The permselectivity of n-butane to i-butane was 10-50 in the range of 30-100℃, which showed practical molecular sieving ability of the formed membranes.
机译:通过水热反应在2.8mm o.d的多孔α-氧化铝载体管的表面上合成ZSM-5型沸石膜。和1.9毫米内径管的平均孔径为约150nm,空隙率为0.45。硅源是二氧化硅细粉,模板是氢氧化四丙基铵和溴化物的混合物。在支撑管上形成的膜中观察到三个区域。顶部区域是多晶沸石层,内部区域是部分填充有沉积物的α-氧化铝大孔层。中间区域是氧化铝颗粒和沉积物的混合物。沸石膜的渗透率随沸石层厚度的减小而增加,但渗透选择性与膜的形态无关。在30-100℃范围内,正丁烷对异丁烷的选择性渗透率为10-50,这表明所形成的膜具有实际的分子筛分能力。

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