脱氢
膜
渗透
选择性
丙烷
沸石
化学工程
催化作用
膜反应器
碳氢化合物
氢
无机化学
化学
材料科学
有机化学
工程类
生物化学
作者
Seok‐Jhin Kim,Yujun Liu,Jason S. Moore,Ravindra S. Dixit,John G. Pendergast,David S. Sholl,Christopher W. Jones,Sankar Nair
标识
DOI:10.1021/acs.chemmater.6b01458
摘要
We demonstrate significantly enhanced conversion and selectivity in high-temperature propane dehydrogenation (PDH) membrane reactors via the synthesis and use of small-pore SAPO-34 zeolite membranes. The reduction of SAPO-34 membrane thickness to ∼1 μm levels while maintaining good H2 selectivity is challenging. Initial reductions in membrane thickness were achieved using a single structure-directing agent (SDA) and concentrated precursor solution, leading to a large permeance increase and good H2/hydrocarbon selectivity. We further show that thinner (∼1 μm) SAPO-34 membranes can be fabricated on a large area (∼18 cm2) tubular ceramic supports by the use of both base and salt forms of the SDA to independently control the SDA concentration and pH. EDX analysis and elemental mapping confirmed the formation of micrometer-thin (∼1 μm) SAPO-34 zeolite membrane layers on α-alumina tubular supports. Micrometer-thin SAPO-34 membranes reach propylene selectivities greater than 80% as well as high propane conversions (65–75% at weight hourly space velocities of 0.1–0.5 h–1), because of their efficient removal of hydrogen generated in the PDH reaction.
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