3
10
R.A. Varin et al. / Journal of Alloys and Compounds 439 (2007) 302–311
al. [7] reported the equilibrium pressure of pure Mg(AlH4)2 in
the 75–95 C range to be between 88 and 130 bar. As a result,
product requires some additional long-time annealing in vac-
uum [19]. Such a long production time may not be well suited
for industrial environment. There is also a problem with the
reversibility of the reaction (7). The reactions (7a) and (7b) are
reversible producing MgH2 and Al but still very sluggish [28].
However, our previous studies [15] suggest that the reaction (3)
between MgH2 and Al to form Mg(AlH4)2 is most likely irre-
versible.
◦
a hydrogen pressure barrier of 41 bar, which we used during
temperature stabilization period in a Sieverts-type apparatus in
the present work might have been insufficient to prevent the
◦
reaction (3) to occur during heating to 150 and 350 C in the
temperature stabilization period, giving rise to some desorption
according to the reaction (3) even before the temperature was
fully stabilized. This explanation is supported by the pressure
increase monitored during temperature stabilization period at
4. Conclusions
◦
1
50 C. Since the pressure increase is due to two factors such
as temperature and hydrogen release then its increment due to
just hydrogen release can be estimated by subtracting the pres-
sure increase due to temperature estimated from the heating
of empty crucible from the pressure registered while heating
crucible containing a powder sample synthesized for 5 h. This
estimate gives ∼1.79 wt.% H2 already released during temper-
A mixture of Mg(AlH4)2 + 2NaCl has been successfully syn-
thesized by the mechano-chemical activation synthesis (MCAS)
of the stoichiometric mixture of 2NaAlH4 and MgCl2 com-
pounds by ball milling for 5 and 10 h in a magneto-mill. The
particle size of the as-milled powder mixture is on the order of
2 m after milling for 5, 10 and 40 h. The Mg(AlH4)2 hydride is
nanocrystalline having the grain size of around 18 nm. Even rela-
tively short milling for just 10 h results in a partial decomposition
of pre-synthesized Mg(AlH4)2 into -MgH2 and the nanocrys-
talline elemental Al (grain size ∼26 nm). Prolonged milling for
40 h results in a complete decomposition of the Mg(AlH4)2 into
nanocrystalline -MgH2 (grain size ∼11 nm) and the elemental
Al (grain size ∼20 nm).
◦
ature stabilization period at 150 C. Therefore, the total amount
of hydrogen desorbed will be the sum of the hydrogen desorbed
during temperature stabilization period (∼1.79 wt.%) and the
hydrogen desorbed in the isothermal desorption period of the
◦
test at 150 C, i.e. 0.45 wt.%. This summation gives the total of
2
◦
.24 wt.% H2 desorbed at 150 C, which is still slightly smaller
than the theoretical 2.98 wt.% H2.
Similar estimate taking into account the pressure increase
DSC test of the Mg(AlH4)2 + 2NaCl mixture synthesized for
5 and 10 h, results in the decomposition of Mg(AlH4)2 into -
◦
calculated from the heating of empty crucible up to 350 C
◦
gives ∼2.5 wt.% H2 desorbed during temperature stabilization
MgH2 + 2Al + 3H2 (+2NaCl) within the range 125–180 C (at
◦
◦
period up to 350 C. Adding this up to the amount of ∼0.75 wt.%
the scan rate of 4 C/min) as confirmed by X-ray diffraction.
desorbed during the isothermal desorption period of the test at
However, thenatureofthistransformationbeingeitherendother-
mic [18,19] or exothermic [20] cannot be unambiguously estab-
lished because a number of samples tested in DSC at the scan
◦
3
50 C (as discussed above) gives us ∼3.25 wt.% of the total
hydrogen desorbed which is still smaller than the total theoret-
ical value of ∼3.97 wt.%H2 stored in the Mg(AlH4)2 + 2NaCl
mixture. We are not sure if this is a pure coincidence but in
◦
rate of 4 and 20 C/min showed both types of transformation,
most likely, owing to a very small enthalpy of decomposi-
tion of Mg(AlH4)2, which is cited in the literature as being
equal to ∼1.7 kJ/molH [19]. Desorption experiments of the
Mg(AlH4)2 + 2NaCl powder synthesized for 5 h, carried out in a
◦
both cases of Sieverts desorption at 150 and 350 C, the total
amount of hydrogen desorbed in the experiment is short of
∼
0.7 wt.% with respect to the theoretical hydrogen capacity val-
◦
ues. Sincethecalibratedaccuracyofdesorbedhydrogencapacity
is about ± 0.2 wt.% H2 in our Sieverts-type apparatus (calibrated
on a commercial MgH2) then the experimental deficiency of
Sieverts-type apparatus at 150 C, show that the total amount of
hydrogen desorbed during temperature stabilization period and
isothermal desorption period is ∼2.24 wt.%.
◦
∼
0.7 wt.% is not due to the experimental error and as such must
DSC test from 180 to 500 C of the Mg(AlH4)2 + 2NaCl mix-
be related to some other factor. One explanation could be that
the powder synthesized for 5 h already lost about ∼0.7 wt.% of
hydrogen due to partial decomposition of Mg(AlH4)2 during
milling. However, this needs further study.
ture synthesized for 5 and 10 h results in three endothermic
◦
reactions with the peak maxima at ∼271, ∼316 and ∼452 C
◦
◦
(at the scan rate of 4 C/min). In the first endo effect at ∼270 C
the -MgH2 hydride decomposes and the free elemental Mg
reacts with the pre-existing free elemental Al forming an equi-
librium mixture of intermetallic compound Al3Mg2 and Al(Mg)
The major problem in the MCAS technology is the forma-
tion of a large amount of waste by-product NaCl. With 2 mol of
NaCl per only 1 mol of Mg(AlH4)2 (reaction (3)) the excellent
theoretical hydrogen capacity ∼9.3 wt.% of pure Mg(AlH4)2 is
reduced to the very inferior theoretical ∼3.97 wt.% H2 in the
mixture of Mg(AlH4)2 + 2NaCl. As reported by Mamatha et al.
◦
solid solution. The nature of the second peak at ∼315 C is not
clear and can be interpreted either as due to the formation of
the Al3Mg2 intermetallic compound or further decomposition
of the remnant -MgH2. Heating of the powder synthesized for
40 h, which contains only a single -MgH2 hydride results in
[
19] it is possible to separate Mg(AlH4)2 from NaCl by the
◦
Soxhlet extraction method which is based on the suspension
of the Mg(AlH4)2 + 2NaCl mixture in the diethyl ether (Et2O)
solvent. However, there are a couple of serious disadvantages of
this extraction method. First, the extracted Mg(AlH4)2 is usually
contaminated with the solvent adduct [20]. Second, the extrac-
tion process needs several days to be completed and then the
two endothermic peaks with the maxima at ∼290 and ∼451 C
◦
(at the scan rate of 4 C/min). The former peak is due to the
decomposition of -MgH2. The endo peaks with the maximum
◦
at 451–452 C, observed in all the synthesized powders, are due
to the eutectic melting of the mixture of Al3Mg2 and Al(Mg)
as required by the binary phase diagram Al–Mg. Desorption