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首页> 外文期刊>Journal of Chemical Engineering of Japan >Preparation of MFI-Type Zeolite Membranes and Their Use in Separating n-Butane and i-Butane
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Preparation of MFI-Type Zeolite Membranes and Their Use in Separating n-Butane and i-Butane

机译:MFI型沸石膜的制备及其在正丁烷和异丁烷分离中的应用

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摘要

References(21) Cited-By(19) MFI-type zeolite membranes were synthesized by hydrothermal reaction on the surface of porous α-alumina support tubes with different pore sizes. The zeolite membranes consisted of three zones: 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 morphology of the zeolite membranes was dependent on the substrates. The permeance of zeolite membranes formed on the substrate possessing pores of 150–170 nm under identical conditions ranged over two orders of magnitude. There was no definite relationship between n-butane/i-butane (n-C4H10/i-C4H10) permselectivity and permeance, although permeance was affected by the substrates. The n-C4H10/i-C4H10 permselectivity calculated from single-component permeances was in the range of 1.5~12 at 100°C, and the activation energy for the permeances was 11 kJ·mol-1. The selectivity increased in the case of n-C14H10 separation from a mixture containing a small amount of i-C4H10. The zeolite membranes thus served as molecular-sieving for C4 isomers.
机译:参考文献(21)引用了By(19)的MFI型沸石膜是通过水热反应在具有不同孔径的多孔α-氧化铝支撑管表面上合成的。沸石膜由三个区域组成: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。沸石膜的形态取决于基底。在相同条件下,形成在具有150-170 nm孔的基材上的沸石膜的渗透率范围达两个数量级。尽管渗透率受底物的影响,但正丁烷/异丁烷(n-C4H10 / i-C4H10)的渗透性与渗透率之间没有明确的关系。由单组分磁导率计算出的n-C4H10 / i-C4H10磁导率在100℃下为1.5〜12,磁导率的活化能为11 kJ·mol-1。从包含少量i-C4H10的混合物中分离n-C14H10时,选择性增加。沸石膜因此用作C4异构体的分子筛。

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