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Hydrogen desorption from the mixture of Mg(NH2)2 and 2LiH presents two pressure-dependent segments at a given temperature – ∼2/3 of the hydrogen is released at relatively higher pressures and forms a pressure plateau and the other 1/3 is desorbed at lower pressures. The overall reaction heat measured in a differential scanning calorimeter is 44.1 kJ/mol H 2, while the heat-of-desorption of H2 in the higher pressure plateau is about 38.9 kJ/mol H2, a favorable thermodynamics for PEM Fuel Cell application. However, the relatively higher activation energy (Ea = 102 kJ/mol) sets a kinetic barrier. © 2005 Elsevier B.V. All rights reserved.

The kinetics of the hydrogen sorption of Ti-doped direct-synthesized NaAlH4 has been studied by measuring sorption rates at various temperatures and applied pressures. Formation and decomposition rate equations for NaAlH4 and Na3AlH6 are proposed, and pre-exponential factors and activation energies have been calculated for these reactions. These equations were used to calculate alanate decomposition curves. The results fit the experimental data very well. The predictive capabilities of this empirical approach provide a very useful modeling tool for optimizing the performance of the alanates over a range of hydrogen absorption temperatures and pressures. Under a typical hydrogen-loading condition (constant pressure), the optimum temperature for “fast fill” can be determined.

An overview is presented of recent advances in the development of new and improved alanates for applications and in the fundamental understanding of how Ti-doping enhances hydrogen absorption. Sample materials were produced using approaches based on direct-synthesis and dry Ti-doping methods. It is desirable to introduce Ti through non-reactive processes to avoid the hydrogen capacity loss that occurs through the formation of inactive byproducts (for example Na–halide from the decomposition of Ti–halides and Na–oxides from the decomposition of Ti–alkoxides). We show, for the first time, that alanates can be Ti-doped using TiH2 or through indirect-doping by pre-reacting TiCl2 with LiH. Both methods result in enhanced kinetics. However, improved rates were achieved only after a prolonged activation period of about a 10 cycles, suggesting that cycling leads to Ti diffusion and substitution into the alanate lattice which provides the mechanism through which Ti-doping enhances kinetics. Thus, the reactive decomposition of Ti–halide and alkoxide precursors in the doping process serves an important but not necessarily required function.

The kinetics of absorption and desorption of hydrogen from NaAlH 4 have previously been shown to improve upon the addition of a catalyst-precursor such as TiCl 3 . In this paper we demonstrate that TiCl 2 , TiF 3 , and TiBr 4 all effectively improve sorption kinetics. Arrhenius data indicate that the catalyst precursors behave in essentially the same manner. Evidently the valency of Ti in the catalyst-precursor is inconsequential to the role of Ti in altering the kinetic mechanism. The formation of TiAl 3 on doping with TiCl 3 has been observed. The presence of TiAl 3 appears to contribute in part to the enhanced kinetics in these systems.

The reversible hydrogen storage properties of Ti-catalyzed NaAlH 4 (and associated Na 3 AlH 6 ) were studied as a function of Ti-content using a dry preparation technique consisting of the ball-milling of NaAlH 4 +TiCl 3 mixtures (0–9 mol.% TiCl 3 ). This process is believed to result in the in situ solid-state introduction of metallic Ti via the reduction of the TiCl 3 by the Na-component of NaAlH 4 (to form NaCl). Properties studied were hydriding and dehydriding rates and reversible gravimetric H-capacity as a function of starting TiCl 3 content. Detailed isothermal kinetic studies were done over a wide temperature range (20–225 °C) and treated by Arrhenius analysis. All kinetics were found to follow the Arrhenius equation and the changes of thermal activation energies and rate constants with TiCl 3 -content were observed that may give valuable insights into the as-yet unknown mechanistic factors that control H 2 desorption and absorption kinetics. Ti increases both dehydriding and hydriding kinetics (and associated practical engineering rates), but at the substantial expense of H-capacity. The finite room temperature decomposition of the catalyzed NaAlH 4 phase was reconfirmed and rates better quantified.

A number of laboratories have now demonstrated that catalyst-assisted NaAlH 4 can reversibly absorb and desorb hydrogen in the solid state at moderate temperatures. An understanding of the mechanisms by which bulk decomposition and reformation of the compound can occur in the presence of a surface catalyst is important to improving the kinetic and thermodynamic properties of alanates for use in hydrogen storage applications. Using scanning electron microscopy (SEM) and energy dispersive spectroscopy (EDS), we have examined the microstructure and elemental composition of Na alanate samples, doped using a liquid Ti/Zr catalyst precursor, for a number of conditions. First, microscopy and compositional analyses were performed at different stages of the decomposition process within the first desorption cycle. Second, the material was characterized after multiple absorption/desorption cycles (five cycles). Finally, the effects of the catalyst doping procedure on particle size, surface morphology and surface composition were examined. Significant changes in particle morphology and in elemental distribution were found to be induced by the desorption and cycling processes. Importantly, our measurements indicate that the initial dehydriding reactions were accompanied by significant enhancement of Al concentration toward the surface of particles and that elemental segregation occurred with repeated absorption/desorption cycles.