The poor kinetics of hydrogen evolution and the irreversibility of the hydrogen discharge hamper the use of transition metal borohydrides as hydrogen storage materials, and the drawbacks of current synthetic methods obstruct the exploration of these systems. A wet-chemistry approach, which is based on solvent-mediated metathesis reactions of precursors containing bulky organic cations and weakly coordinating anions, leads to mixed-metal borohydrides that contain only a small amount of "dead mass". The applicability of this method is exemplified by Li[Zn 2 (BH 4 ) 5 ] and M[Zn(BH 4 ) 3 ] salts (M = Na, K), and its extension to other systems is discussed.The efficient storage of hydrogen is one of the most pressing problems related to utilization of the lightest element as an energy carrier. [1] Metal borohydrides contain large amounts of hydrogen compared to other groups of inorganic compounds (up to 24.5 wt % for NH 4 BH 4 ) [2] and have been intensely examined as potential materials for hydrogen storage. [3] The properties of metal borohydrides that limit their applicability as hydrogen storage materials (such as temperature of H 2 release [4] and reversibility) can be tuned-up to some extent by the substitution at the metal or ligand site or by the preparation of complex materials, [5] e.g. LiK(BH 4 ) 2 , [4] M[Sc-(BH 4 ) 4 ], M = Li, Na, K, [6] Li 3 MZn 5 (BH 4 ) 15 , M = Mg, Mn. [7] The most frequently used synthetic pathway toward unsolvated single-and mixed-metal borohydrides consists of a mechanochemical reaction between a metal halide and an alkali metal borohydride. [3] For example:The method can be easily extended to mixtures of the three substrates.The mechanochemical (high-energy milling) method, although very convenient for the initial screening of a wide variety of single-and mixed-metal borohydrides, [10] has serious drawbacks, which hamper the application of this method on an industrial scale. One key disadvantage is the presence of halide-containing by-products in the sample [Equations (1) [8] and (2) [9] ]. This "dead mass" usually constitutes 40-60 wt % of the composite, which dramatically decreases the effective hydrogen content and often influences the thermal decomposition process, for example, through the formation of halide-substituted borohydrides. [6c, 11] For example, the total hydrogen content of Li[Zn 2 (BH 4 ) 5 ] decreases from 9.5 wt % to less than 5.3 wt % (i.e. below the 2017 US Department of Energy limit of 5.5 wt %) for the composite product obtained according to Equation (2). The separation methods based on the difference of buoyancy of the products or solubility of borohydrides in ethereal solvents either do not work or lead to ether-solvated products. [12] Most ethers contribute even more to the dead mass than alkali metal halides, they compromise the purity of the evolved H 2 gas, and they often cannot be removed without thermal decomposition of the borohydrides, especially those which evolve H 2 in the desirable low-temperature range (60-100 8C). [13] On the other hand, ...