共 50 条
Catalyzed LiBH4 and MgH2 mixture for hydrogen storage
被引:51
|作者:
Sridechprasat, Pattaraporn
[1
]
Suttisawat, Yindee
[1
]
Rangsunvigit, Pramoch
[1
]
Kitiyanan, Boonyarach
[2
]
Kulprathipanja, Santi
[3
]
机构:
[1] Chulalongkorn Univ, Petr & Petrochem Coll, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Ctr Petr Petrochem & Adv Mat, Bangkok 10330, Thailand
[3] UOP, Des Plaines, IL 60017 USA
关键词:
LiBH4;
MgH2;
Catalyst;
Hydrogen storage;
DESTABILIZATION;
PERFORMANCES;
COMPOSITES;
MAGNESIUM;
D O I:
10.1016/j.ijhydene.2010.07.003
中图分类号:
O64 [物理化学(理论化学)、化学物理学];
学科分类号:
070304 ;
081704 ;
摘要:
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.
引用
收藏
页码:1200 / 1205
页数:6
相关论文