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The Effect of Impurities on Permeance through Chabazite Zeolite Membranes

机译:杂质对菱沸石沸石膜通透性的影响

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摘要

Zeolite membranes selectively permeate gases based on differences in size, diffusivity, and loading. The chabazite zeolites SAPO-34 and SSZ-13 have 0.38-nm pores, which make them suitable for separating CO2 (0.33-nm kinetic diameter) from CH4 (0.38 nm) for natural gas purification. Natural gas also contains ethane, propane, butane, and higher hydrocarbon impurities that can adsorb in the membranes and affect their performance.;We studied the effect of small alkanes on H2/N2 separations in SAPO-34 by adding ethane, propane, or n-butane to the feed. Propane reduced the permeance of both gases, but it reduced the H2 permeance less than the N2 permeance, so that the selectivity increased from about 4 to about 9. n-Butane had a similar effect, but ethane caused no change in selectivity. Reduced H2 loading due to competitive adsorption would decrease H2/N2 selectivity if competitive adsorption were the dominant mechanism. Therefore, diffusion plays a significant role and the alkanes must have decreased N2 diffusivity more than H2 diffusivity.;We studied the effects of toluene, which is too large (0.59 nm) to diffuse into zeolite pores, on CO2 and N2 permeance through SAPO-34 membranes. When 0.65 mol% toluene was added to the feed, the CO 2 permeance decreased by 45% and the N2 permeance decreased by 50% at 172-kPa pressure. At 10-kPa feed pressure, 8.5% toluene decreased CO2 permeance by 20%. Binary isotherm models predict that competitive adsorption between toluene and CO2 on the external surface significantly reduced the CO2 coverage, and thus the driving force for CO 2 transport.;Finally, we measured the effect of C1 through C4 alkanes on CO2 permeance through SSZ-13 membranes. Propane and n-butane have kinetic diameters (0.43 nm) larger than the SSZ-13 pores, but they adsorb to high loadings in SSZ-13 crystals because these molecules are flexible. Methane decreased CO2 permeance by 5%, and ethane decreased CO2 permeance by 45% at the same concentration. Propane, however, only decreased CO2 permeance by 10%, and n-butane decreased the permeance by 15%. Apparently, the larger alkanes did not adsorb into the SSZ-13 pores, likely due to an altered external pore structure, and propane and n-butane only reduced CO2 permeance by adsorbing on the external surface.
机译:沸石膜根据尺寸,扩散率和载量的差异选择性渗透气体。菱沸石沸石SAPO-34和SSZ-13具有0.38 nm的孔,这使其适合于从CH4(0.38 nm)中分离出CO2(0.33 nm的动力学直径)进行天然气净化。天然气中还包含乙烷,丙烷,丁烷和可吸附在膜上并影响其性能的高级烃杂质。;我们通过添加乙烷,丙烷或正己烷,研究了小烷烃对SAPO-34中H2 / N2分离的影响。 -丁烷进料。丙烷降低了两种气体的渗透率,但降低了H2渗透率,但降低了N2渗透率,因此选择性从大约4增加到大约9。正丁烷具有相似的作用,但是乙烷不会引起选择性变化。如果竞争性吸附是主要机理,则由于竞争性吸附而降低的H2负荷将降低H2 / N2的选择性。因此,扩散起着重要作用,烷烃必须比H2扩散降低更多的N2扩散。;我们研究了甲苯(0.59 nm)太大而无法扩散到沸石孔中的甲苯通过SAPO-对CO2和N2渗透的影响。 34个膜。当将0.65mol%的甲苯加入进料中时,在172kPa压力下,CO 2渗透率降低了45%,N 2渗透率降低了50%。在10kPa进料压力下,8.5%的甲苯会使CO2渗透率降低20%。二元等温线模型预测,甲苯和二氧化碳在外表面上的竞争性吸附会显着降低二氧化碳的覆盖率,从而降低二氧化碳的运输动力。最后,我们测量了C1到C4烷烃对通过SSZ-13渗透CO2的影响。膜。丙烷和正丁烷的动力学直径(0.43 nm)大于SSZ-13孔,但由于这些分子具有柔韧性,因此它们吸附到SSZ-13晶体中的高载荷下。在相同浓度下,甲烷会使CO2渗透率降低5%,而乙烷会使CO2渗透率降低45%。但是,丙烷仅会使CO2渗透率降低10%,正丁烷使渗透率降低15%。显然,较大的烷烃可能不会吸附到SSZ-13孔中,这可能是由于外部孔结构发生了变化,丙烷和正丁烷仅通过吸附在外表面上而降低了CO2的透过率。

著录项

  • 作者

    Chisholm, Nicholas Odell.;

  • 作者单位

    University of Colorado at Boulder.;

  • 授予单位 University of Colorado at Boulder.;
  • 学科 Chemical engineering.;Energy.
  • 学位 Ph.D.
  • 年度 2017
  • 页码 192 p.
  • 总页数 192
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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