Silver-exchanged zeolite LTA molecular sieving membranes with enhanced hydrogen selectivity

Research output: Contribution to journalArticleResearchpeer review

Authors

  • Kai Xu
  • Chenfang Yuan
  • Jürgen Caro
  • Aisheng Huang

External Research Organisations

  • Chinese Academy of Sciences (CAS)
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Details

Original languageEnglish
Pages (from-to)1-8
Number of pages8
JournalJournal of membrane science
Volume511
Early online date24 Mar 2016
Publication statusPublished - 1 Aug 2016

Abstract

In the present work, we report a new road to enhance the gas separation performances of the zeolite Na-LTA membrane by tuning the pore size of zeolite LTA through silver cation exchange. Through the functionalization of the alumina support by using 3-aminopropyltriethoxysilane (APTES), a thin, phase-pure and well intergrown zeolite Na-LTA membrane with a thickness of about 5.0 μm can be facilely prepared on the APTES-modified macroporous α-Al2O3 tube. After a following silver exchange treatment of the as-synthesized zeolite Na-LTA membranes, the sodium ions in zeolite Na-LTA framework are replaced by silver ions, thus forming zeolite Ag-LTA membranes with a narrower pore diameter. The zeolite Ag-LTA membranes were characterized by scanning electron microscopy (SEM), X-ray diffraction (XRD), and X-ray photoelectron spectroscopy (XPS). It is found that both the morphology and structure of the zeolite Na-LTA membrane keep unchanged after silver-exchange, and no cracks, pinholes or other defects are observed in the membrane layer. The zeolite Ag-LTA membrane shows high hydrogen selectivity due to the reduction of pore size of the zeolite Ag-LTA. For the separation of the binary mixture at 50 °C and 2.0 bar, the separation factor of H2/C3H8 is α≈120.8, which by far exceeds α≈19.4 of the starting Na-LTA membrane, and are also much higher than the separation factors previously reported for the H2/C3H8 mixture on zeolite membranes.

Keywords

    Gas separation, Ion exchange, Molecular sieve membrane, Zeolite Ag-LTA membrane, Zeolite LTA membrane

ASJC Scopus subject areas

Cite this

Silver-exchanged zeolite LTA molecular sieving membranes with enhanced hydrogen selectivity. / Xu, Kai; Yuan, Chenfang; Caro, Jürgen et al.
In: Journal of membrane science, Vol. 511, 01.08.2016, p. 1-8.

Research output: Contribution to journalArticleResearchpeer review

Xu K, Yuan C, Caro J, Huang A. Silver-exchanged zeolite LTA molecular sieving membranes with enhanced hydrogen selectivity. Journal of membrane science. 2016 Aug 1;511:1-8. Epub 2016 Mar 24. doi: 10.1016/j.memsci.2016.03.036
Xu, Kai ; Yuan, Chenfang ; Caro, Jürgen et al. / Silver-exchanged zeolite LTA molecular sieving membranes with enhanced hydrogen selectivity. In: Journal of membrane science. 2016 ; Vol. 511. pp. 1-8.
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AU - Xu, Kai

AU - Yuan, Chenfang

AU - Caro, Jürgen

AU - Huang, Aisheng

PY - 2016/8/1

Y1 - 2016/8/1

N2 - In the present work, we report a new road to enhance the gas separation performances of the zeolite Na-LTA membrane by tuning the pore size of zeolite LTA through silver cation exchange. Through the functionalization of the alumina support by using 3-aminopropyltriethoxysilane (APTES), a thin, phase-pure and well intergrown zeolite Na-LTA membrane with a thickness of about 5.0 μm can be facilely prepared on the APTES-modified macroporous α-Al2O3 tube. After a following silver exchange treatment of the as-synthesized zeolite Na-LTA membranes, the sodium ions in zeolite Na-LTA framework are replaced by silver ions, thus forming zeolite Ag-LTA membranes with a narrower pore diameter. The zeolite Ag-LTA membranes were characterized by scanning electron microscopy (SEM), X-ray diffraction (XRD), and X-ray photoelectron spectroscopy (XPS). It is found that both the morphology and structure of the zeolite Na-LTA membrane keep unchanged after silver-exchange, and no cracks, pinholes or other defects are observed in the membrane layer. The zeolite Ag-LTA membrane shows high hydrogen selectivity due to the reduction of pore size of the zeolite Ag-LTA. For the separation of the binary mixture at 50 °C and 2.0 bar, the separation factor of H2/C3H8 is α≈120.8, which by far exceeds α≈19.4 of the starting Na-LTA membrane, and are also much higher than the separation factors previously reported for the H2/C3H8 mixture on zeolite membranes.

AB - In the present work, we report a new road to enhance the gas separation performances of the zeolite Na-LTA membrane by tuning the pore size of zeolite LTA through silver cation exchange. Through the functionalization of the alumina support by using 3-aminopropyltriethoxysilane (APTES), a thin, phase-pure and well intergrown zeolite Na-LTA membrane with a thickness of about 5.0 μm can be facilely prepared on the APTES-modified macroporous α-Al2O3 tube. After a following silver exchange treatment of the as-synthesized zeolite Na-LTA membranes, the sodium ions in zeolite Na-LTA framework are replaced by silver ions, thus forming zeolite Ag-LTA membranes with a narrower pore diameter. The zeolite Ag-LTA membranes were characterized by scanning electron microscopy (SEM), X-ray diffraction (XRD), and X-ray photoelectron spectroscopy (XPS). It is found that both the morphology and structure of the zeolite Na-LTA membrane keep unchanged after silver-exchange, and no cracks, pinholes or other defects are observed in the membrane layer. The zeolite Ag-LTA membrane shows high hydrogen selectivity due to the reduction of pore size of the zeolite Ag-LTA. For the separation of the binary mixture at 50 °C and 2.0 bar, the separation factor of H2/C3H8 is α≈120.8, which by far exceeds α≈19.4 of the starting Na-LTA membrane, and are also much higher than the separation factors previously reported for the H2/C3H8 mixture on zeolite membranes.

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KW - Ion exchange

KW - Molecular sieve membrane

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KW - Zeolite LTA membrane

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