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A hybrid zeolitic imidazolate framework Co-IM-mIM membrane for gas separation

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【作者】 高正才李立清李海龙陈若菲WANG S王阳刚

【Author】 GAO Zheng-cai;LI Li-qing;LI Hai-long;CHEN Ruo-fei;WANG S;WANG Yang-gang;School of Energy Science and Engineering, Central South University;Department of Chemical Engineering, Curtin University;School of Physical Science and Technology, Lanzhou University;

【机构】 School of Energy Science and Engineering Central South UniversityDepartment of Chemical Engineering Curtin UniversitySchool of Physical Science and Technology Lanzhou University

【摘要】 A zeolitic imidazolate hybrid membrane(Co-IM-mIM) containing two imidazolate ligands deposited on a macroporous α-alumina support was prepared by pre-depositing and secondary growth technique. XRD, TGA and SEM characterizations demonstrate that a stable and thin, but dense and pure-phase Co-IM-mIM membrane can be obtained on the macroporous-alumina discs in Teflon-lined autoclave at 120 °C after pre-depositing by dip-coating at room temperature. No visible cracks, pinholes or other defects were observed on the membrane layer. The gas separation studies of Co-IM-mIM membrane were carried out at 25 °C and 1×105 Pa, showing ideal selectivity of 6.95, 5.25, 3.40 for H2/CO2, H2/N2 and H2/CH4, respectively, and a permeance of 17.37× 10-6 mol/(m2·s·Pa) for H2. The influence of temperature and trans-membrane pressure on hydrogen separation and permeation was also carried out. The gas permeation and selectivity demonstrate that this membrane may have potential applications for efficient H2 separation.

【Abstract】 A zeolitic imidazolate hybrid membrane(Co-IM-mIM) containing two imidazolate ligands deposited on a macroporous α-alumina support was prepared by pre-depositing and secondary growth technique. XRD, TGA and SEM characterizations demonstrate that a stable and thin, but dense and pure-phase Co-IM-mIM membrane can be obtained on the macroporous-alumina discs in Teflon-lined autoclave at 120 °C after pre-depositing by dip-coating at room temperature. No visible cracks, pinholes or other defects were observed on the membrane layer. The gas separation studies of Co-IM-mIM membrane were carried out at 25 °C and 1×105 Pa, showing ideal selectivity of 6.95, 5.25, 3.40 for H2/CO2, H2/N2 and H2/CH4, respectively, and a permeance of 17.37× 10-6 mol/(m2·s·Pa) for H2. The influence of temperature and trans-membrane pressure on hydrogen separation and permeation was also carried out. The gas permeation and selectivity demonstrate that this membrane may have potential applications for efficient H2 separation.

【基金】 Project(21376274)supported by the National Natural Science Foundation China;Project(2015BAL04B02)supported by the National Key Technology R&D Program of China
  • 【文献出处】 Journal of Central South University ,中南大学学报(英文版) , 编辑部邮箱 ,2017年08期
  • 【分类号】TQ051.893
  • 【被引频次】1
  • 【下载频次】20
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