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

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autoren

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

Externe Organisationen

  • Chinese Academy of Sciences (CAS)
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Details

OriginalspracheEnglisch
Seiten (von - bis)1-8
Seitenumfang8
FachzeitschriftJournal of membrane science
Jahrgang511
Frühes Online-Datum24 März 2016
PublikationsstatusElektronisch veröffentlicht (E-Pub) - 24 März 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.

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Silver-exchanged zeolite LTA molecular sieving membranes with enhanced hydrogen selectivity. / Xu, Kai; Yuan, Chenfang; Caro, Jürgen et al.
in: Journal of membrane science, Jahrgang 511, 24.03.2016, S. 1-8.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-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 Mär 24;511:1-8. Epub 2016 Mär 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 ; Jahrgang 511. S. 1-8.
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TY - JOUR

T1 - Silver-exchanged zeolite LTA molecular sieving membranes with enhanced hydrogen selectivity

AU - Xu, Kai

AU - Yuan, Chenfang

AU - Caro, Jürgen

AU - Huang, Aisheng

PY - 2016/3/24

Y1 - 2016/3/24

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.

KW - Gas separation

KW - Ion exchange

KW - Molecular sieve membrane

KW - Zeolite Ag-LTA membrane

KW - Zeolite LTA membrane

UR - http://www.scopus.com/inward/record.url?scp=84961875196&partnerID=8YFLogxK

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DO - 10.1016/j.memsci.2016.03.036

M3 - Article

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JO - Journal of membrane science

JF - Journal of membrane science

SN - 0376-7388

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