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Characterization of Pd 60 Cu 40 Composite Membrane Prepared by a Reverse Build-Up Method for Hydrogen Purification

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  • Yasunari Shinoda

    (Department of Chemical Science and Engineering, School of Materials and Chemical Technology, Tokyo Institute of Technology, 2-12-1, Ōokayama, Meguro-ku, Tokyo 152-8550, Japan)

  • Masakazu Takeuchi

    (Department of Chemical Science and Engineering, School of Materials and Chemical Technology, Tokyo Institute of Technology, 2-12-1, Ōokayama, Meguro-ku, Tokyo 152-8550, Japan)

  • Hikaru Mizukami

    (Department of Transdisciplinary Science and Engineering, School of Environment and Society, Tokyo Institute of Technology, 2-12-1, Ōokayama, Meguro-ku, Tokyo 152-8550, Japan)

  • Norikazu Dezawa

    (Sanno Co., Ltd., 5-8-8, Tsunashima-Higashi, Kouhoku-ku, Yokohama 223-0052, Japan)

  • Yasuhiro Komo

    (Sanno Co., Ltd., 5-8-8, Tsunashima-Higashi, Kouhoku-ku, Yokohama 223-0052, Japan)

  • Takuya Harada

    (Department of Chemical Science and Engineering, School of Materials and Chemical Technology, Tokyo Institute of Technology, 2-12-1, Ōokayama, Meguro-ku, Tokyo 152-8550, Japan)

  • Hiroki Takasu

    (Laboratory for Zero-Carbon Energy, Institute of Innovative Research, Tokyo Institute of Technology (Tokyo Tech), 2-12-1, Ōokayama, Meguro-ku, Tokyo 152-8550, Japan)

  • Yukitaka Kato

    (Laboratory for Zero-Carbon Energy, Institute of Innovative Research, Tokyo Institute of Technology (Tokyo Tech), 2-12-1, Ōokayama, Meguro-ku, Tokyo 152-8550, Japan)

Abstract

A thin Pd-based H 2 -permeable membrane is required to produce high-purity H 2 with high efficiency. In this study, a porous Ni-supported Pd 60 Cu 40 composite H 2 -permeable membrane was developed using a reverse build-up method to produce economical H 2 purification. The thickness of the Pd 60 Cu 40 alloy layer produced by the improved membrane production process reached 1.0 μm; it was thinner than the layer obtained in a previous study (3.7 μm). The membrane was characterized by scanning electron microscope, inductively coupled plasma optical emission spectrometer, H 2 permeation test, and Auger microprobe analysis. The permeation tests were performed at 300–320 °C and 50–100 kPa with H 2 introduced from the primary side. The H 2 permeation flux was stable up to ~320 °C. The n -value was determined to be 1.0. The H 2 permeance of the membrane was 2.70 × 10 −6 mol m −2 s −1 Pa −1.0 at 320 °C, after 30 h, similar to those of other 2.2-µm-thick and 3.7-µm-thick Pd 60 Cu 40 composite membranes, suggesting that the adsorption and dissociation reaction processes on the PdCu alloy surface were rate-limiting. The Pd cost of the membrane was estimated to be ~1/30 of the Pd cost of the pure Pd 60 Cu 40 membrane.

Suggested Citation

  • Yasunari Shinoda & Masakazu Takeuchi & Hikaru Mizukami & Norikazu Dezawa & Yasuhiro Komo & Takuya Harada & Hiroki Takasu & Yukitaka Kato, 2021. "Characterization of Pd 60 Cu 40 Composite Membrane Prepared by a Reverse Build-Up Method for Hydrogen Purification," Energies, MDPI, vol. 14(24), pages 1-16, December.
  • Handle: RePEc:gam:jeners:v:14:y:2021:i:24:p:8262-:d:697772
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    References listed on IDEAS

    as
    1. Mi Yeon Byun & Ji Sun Kim & Jae Ho Baek & Dae-Won Park & Man Sig Lee, 2019. "Liquid-Phase Hydrogenation of Maleic Acid over Pd/Al 2 O 3 Catalysts Prepared via Deposition–Precipitation Method," Energies, MDPI, vol. 12(2), pages 1-8, January.
    2. Hamish Andrew Miller & Jacopo Ruggeri & Andrea Marchionni & Marco Bellini & Maria Vincenza Pagliaro & Carlo Bartoli & Andrea Pucci & Elisa Passaglia & Francesco Vizza, 2018. "Improving the Energy Efficiency of Direct Formate Fuel Cells with a Pd/C-CeO 2 Anode Catalyst and Anion Exchange Ionomer in the Catalyst Layer," Energies, MDPI, vol. 11(2), pages 1-12, February.
    3. Muhammad Abdul Qyyum & Yus Donald Chaniago & Wahid Ali & Hammad Saulat & Moonyong Lee, 2020. "Membrane-Assisted Removal of Hydrogen and Nitrogen from Synthetic Natural Gas for Energy-Efficient Liquefaction," Energies, MDPI, vol. 13(19), pages 1-18, September.
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