In this work, reactions of either LiBH4, ZnCl2 or Zn3N2 with LiNH2 have been studied.
The presence of CoO significantly affected the products and hydrogen release on heating mixtures of
χLiBH4-γLiNH2. The ratios of the l41/amd and the P21/c polymorphs of Li3BN2 in the products have been changed under different conditions studied. On addition of CoO, the temperature of hydrogen release from the χLiBH4-γLiNH2 systems was greatly reduced, starting from 100°C and peaking around 250°C, much lower than 240°C and 330°C without catalyst. Ball-milling helped to improve the amounts of hydrogen desorbed from 3–4 wt% up to ≥10 wt%.
In the reactions of ZnCl2 + nLiNH2 (where n = 2–6), main products were LiCl, Zn3N2, and LiZnN. NH3 was the main gas released from these reactions and the addition of LiH changed NH3 into H2, which was released around 90°C, much lower than in the absence of LiH. A mixture of LiZnN and LiCl obtained from this reaction was partly rehydrogenated to form Li2NH and Zn.
The reaction of Zn3N2 and LiNH2 was found to produce pure LiZnN without LiCl. Neither pure LiZnN nor Zn3N2 could be hydrogenated under the conditions tried, but a mixture resulting from the reaction could react with H2 to form LiNH2 and Zn. The cyclability of the Li–Zn–N system showed an ability to release and take up gases under different pressure conditions. Mg-doping in LiZnN was examined to improve reversibility of the Li–Zn–N system but was not successful