2007
DOI: 10.1016/j.ijhydene.2006.07.020
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Catalytic effect of Zr and Hf on hydrogen desorption/absorption of NaAlH4 and LiAlH4

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Cited by 63 publications
(42 citation statements)
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“…Moreover, the initial desorption temperature of LiAlH 4 remarkably decreased to 58°C by doping 5 mol % NiFe 2 O 4 nanopowders, which is quite lower than that of LiAlH 4 with the addition of other various previously reported catalysts. 4,5,[17][18][19][20]24,26,30,31 Meanwhile, combining these two considerations from the initial dehydrogenation temperature and hydrogen release capability, the optimal content of NiFe 2 O 4 additive of the doped sample with the best dehydrogenation performance is 3 mol %, and the LiAlH 4 +3 mol % NiFe 2 O 4 sample will be utilized for analyzing the catalytic effect and mechanism of NiFe 2 O 4 in the following tests. Although NiFe 2 O 4 nanopowder has exhibited superior catalytic performance by declining the onset dehydrogenation temperature of LiAlH 4 , the reversibility of the completely dehydrogenated 3 mol % doped sample cannot be tested at 140°C under 6.5 MPa hydrogen pressure, as shown in Figure S1 (Supporting Information), resulting from the thermodynamic properties of LiAlH 4 .…”
Section: Resultsmentioning
confidence: 99%
“…Moreover, the initial desorption temperature of LiAlH 4 remarkably decreased to 58°C by doping 5 mol % NiFe 2 O 4 nanopowders, which is quite lower than that of LiAlH 4 with the addition of other various previously reported catalysts. 4,5,[17][18][19][20]24,26,30,31 Meanwhile, combining these two considerations from the initial dehydrogenation temperature and hydrogen release capability, the optimal content of NiFe 2 O 4 additive of the doped sample with the best dehydrogenation performance is 3 mol %, and the LiAlH 4 +3 mol % NiFe 2 O 4 sample will be utilized for analyzing the catalytic effect and mechanism of NiFe 2 O 4 in the following tests. Although NiFe 2 O 4 nanopowder has exhibited superior catalytic performance by declining the onset dehydrogenation temperature of LiAlH 4 , the reversibility of the completely dehydrogenated 3 mol % doped sample cannot be tested at 140°C under 6.5 MPa hydrogen pressure, as shown in Figure S1 (Supporting Information), resulting from the thermodynamic properties of LiAlH 4 .…”
Section: Resultsmentioning
confidence: 99%
“…In the case of the doped mixture, as shown in Figures 4b-e, Al is observed after the milling process. It is possible that the milling process and a dopant might destabilize the structure of LiAlH 4 [9]. After the hydrogen desorption at 300 °C ( Figure 5), Al and LiH are present in both undoped and doped mixtures, without the formation of AlB 2 .…”
Section: Resultsmentioning
confidence: 99%
“…The formation of LiCl might deteriorate the hydrogen desorption ability of the samples, consequently decreasing the hydrogen desorption capacity. The LiAlH 4 and LiBH 4 mixtures doped with TiO 2 , TiCl 3 , VCl 3 , or ZrCl 4 partially decompose during the milling process because the structure of LiAlH 4 is unstable and the additives might destabilize its structure [9]. These metal catalysts in the hydride systems are reduced by the metal hydrides and transformed to TM-neutral [6,18], as shown in Reactions (1) and (2), where TM is the transition metal, M is the metal, and X can be either V or Ti:…”
Section: Resultsmentioning
confidence: 99%
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“…For NaAlH 4 , Bogdanovi c and Schwickardi [1] could show that the addition of a catalyst enhances the kinetics, lowers the decomposition temperature, and, most importantly, makes the rehydrogenation of the compound feasible. The influence of both high energy ball milling and the presence of catalysts on the stability of LiAlH 4 has been the topic of several publications [77][78][79][80][81][82][83][84]. The presence of catalysts accelerates the decomposition of LiAlH 4 and complete decomposition to the hexahydride is observed already after 5 min of ball milling with TiCl 4 (3 wt.%) as catalyst [81].…”
Section: Role Of Catalystsmentioning
confidence: 99%