4.7 Article

Catalyzed LiBH4 and MgH2 mixture for hydrogen storage

Journal

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume 36, Issue 1, Pages 1200-1205

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2010.07.003

Keywords

LiBH4; MgH2; Catalyst; Hydrogen storage

Funding

  1. National Science and Technology Development Agency
  2. Royal Jubilee Ph.D. Program [PHD/0249/2549]
  3. Thailand Research Fund
  4. Petroleum and Petrochemical College (PPC)
  5. Research Unit for Petrochemical and Environment Catalysis, Ratchadapisak Somphot Endowment
  6. Center for Petroleum, Petrochemicals, and Advanced Materials, Chulalongkorn University
  7. UOP, A Honeywell Company, USA

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The hydrogen desorption/absorption of the 2:1 mole ratio of LiBH4 and MgH2 with and without a catalyst was investigated. In the case of the uncatalyzed LiBH4/MgH2 mixture, the first hydrogen desorption started at 50 degrees C. The amount of released hydrogen was 8.6 wt% at the first hydrogen desorption and dramatically reduced to 1.8 wt% at the tenth hydrogen desorption. The decrease in the hydrogen capacity in the subsequent hydrogen desorption may be due to the irreversibility of LiBH4. To investigate effects of a catalyst on the hydrogen desorption, 3 mol% of TiCl3, HfCl4, ZrCl4, or VCl3 was added to the LiBH4/MgH2 mixture. The lowest hydrogen desorption temperature, 260 degrees C, was from the sample with TiCl3. An amount of the catalyst also influenced the kinetics of the hydride mixture and 5 mol% seems to be an optimum amount of TiCl3 that resulted in the lowest hydrogen desorption temperature, 240 degrees C. In addition, the higher the amount of a catalyst, the lower the amount of the released hydrogen. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.

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