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载体改性制备SAPO-34分子筛膜及其H_2/CO_2分离性能的研究

SAPO-34 membrane synthesized on modified carrier and its separation performance for H_2/CO_2
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摘要 以四乙基氢氧化铵(TEAOH)为模板剂,采用传统水热法合成粒径为纳米级SAPO-34分子筛。利用γ-甲基丙烯酰氧基丙基三甲氧基硅烷(KH-570)对载体表面进行改性,再用二次生长法在改性载体上成功制备出高性能SAPO-34分子筛膜。通过X-射线衍射(XRD)和扫描电子显微镜(SEM)对合成的SAPO-34分子筛以及SAPO-34分子筛膜进行表征。结果表明,制备出的SAPO-34分子筛膜连续致密,且结晶度高。对SAPO-34分子筛膜进行气体分离测试以评价其性能,在298 K,膜两侧压差为0.1 MPa条件下,SAPO-34分子筛膜对H_2/CO_2的分离选择性从1.45提高到6.20,CO_2的渗透率也高达1.76×10^(-7)mol/(m^2·s·Pa)。 The nano-scale SAPO-34 zeolites are synthesized by hydrothermal method using tetraethyl ammonium hydroxide( TEAOH) as structure directing agent. The surface of carrier is modified by γ-( methacryloyloxy) propyl trimethoxysilane( KH-570) and then high performance SAPO-34 zeolites membranes are prepared on the modified carrier through secondary growth method.The prepared SAPO-34 zeolite and SAPO-34 zeolite membrane are characterized by X-ray diffraction( XRD) and scanning electron microscopy( SEM). The results show that the prepared SAPO-34 membranes are continuous and compact,and of high crystallinity. The gas separation test is carried out for SAPO-34 zeolite membrane in order to evaluate its performance. At 298 K and a trans-membrane pressure of 0. 1 MPa,the separation selective factor of SAPO-34 membranes against H2/CO2 increases from 1. 45 to 6. 20,and CO2 permeability is also as high as 1. 76×10^(-7)mol/( m^2·s·Pa).
出处 《现代化工》 CAS CSCD 北大核心 2017年第9期119-122,共4页 Modern Chemical Industry
基金 武汉工程大学研究生教育创新基金项目(CX2015084)
关键词 SAPO-34 分子筛膜 改性 H2/CO2 SAPO-34 zeolite membrane modification H2/CO2
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参考文献1

  • 1徐如人,庞文琴,霍启升著..分子筛与多孔材料化学 第2版[M].北京:科学出版社,2015:725.

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