Fig. 3 Dehydrogenation of SBAB/AB mixture using 1 mol% catalyst
at 80 1C in IL.
borazine and polyborazylene in ether solvents,15 we were
unable to prevent polymer formation by catalyst control in
the SBAB solvent. As earlier studies with Ni N-heterocyclic
carbene catalysts showed drastic variation in AB
dehydrogenation selectivity in different solvents,20 several
co-solvents were investigated with AB/SBAB mixtures. In
other investigations we recently found that insoluble poly-
(aminoborane) formation could be avoided with Ru catalyst
precursor 3 using ionic liquid solvents with moderately
coordinating anions such as (EMIM)[EtSO4] (EMIM = 1-ethyl-
3-methylimidazolium).17 Indeed, while diglyme and sulfolane
co-solvents offered no selectivity improvements, dehydrogenation
of equimolar AB and SBAB in (EMIM)[EtSO4] released
3.4 wt% H2 at 80 1C over 4 h without formation of insoluble
poly(aminoborane) (Fig. 3 and S18, ESIw). Gas burette
measurements confirmed formation of additional hydrogen
(Table S1, ESIw; 1.0 equivalent of H2 released in 20 min and
1.7 equivalents of H2 after a reaction period of 3 h) although
with reduced total storage capacity due to the ionic liquid. While
results have not yet been optimized, a (6 : 18 : 15 : 1) liquid
mixture by weight of AB : SBAB : EMIM : RuCl2(PMe3)4
afforded 3.6 wt% H2 in 18 h at 80 1C.
Fig. 1 H2 release from SBAB using 1 mol% catalyst at 60 1C.
Table 1 Metal-catalysed SBAB dehydrogenation at 60 1C
Catalyst
Time/h
Equivalents H2
[Rh(1,5-cod)(m-Cl)]2(1)
[RuCl2{tBu2PCH2CH2NH2}2] (2)
RuCl2(PMe3)4 (3)
20
23
23
1.03
1.55
1.06
Turning next to SBAB/AB solutions, we noted firstly that
AB dehydrogenation was rapid even at 60 1C (Fig. S9, ESIw)
with complete conversion to borazine and polyborazylene;
an effect that persisted even on dilution with sulfolane
(Fig. S10, ESIw), but not in sulfolane without SBAB
(Fig. S11, ESIw). Moreover, no evidence was obtained for
any mixed dehydrogenation products. Metal-catalysed reactions
at the same temperature afforded a total of 3.5 wt% of H2
after 5 h (Fig. 2) and 4.5 wt% after 23 h (Table S1, ESIw) with
0.8–1.0 equivalents of H2 evolving from the system after a 5 h
initial period. Interestingly, catalyst 3 afforded >5.0 wt% of
H2 in 1 h at 80 1C based on SBAB and AB (Fig. 3) and also
gave 1.0 equivalents of H2 in 10 min (Fig. S17, ESIw). While
titania-supported Ni and Fe heterogeneous catalysts showed
little enhancement for dehydrogenation of SBAB/AB
mixtures, Ni on boron nitride afforded 5.3 wt% in 4 h
(Fig. S19 and S20, ESIw) but only 5.7 wt% in 23 h, suggestive
of product inhibition or catalyst poisoning.18
Current work is focused on optimizing these amine-borane/
IL liquid fuel blends, identifying active, long-lived heterogeneous
catalysts21 and conducting analysis of hydrogen purity and
fuel regeneration studies.
We thank the US Department of Energy, Energy Efficiency
and Renewable Energy office for support of this work through
the Chemical Hydrogen Storage Center of Excellence, the
University of Ottawa’s NMR core facility and Dr William
R. H. Wright for technical assistance.
Notably, all these reactions were accompanied by formation
of a white precipitate that was insoluble in tetrahydrofuran,
indicative of linear poly(aminoborane), (NH2BH2)n.19 While
previous work indicated that catalyst 1 yields primarily
Notes and references
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¨
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M. Mitoraj, Ł. Pieko, A. Michalak, S.-J. Hwang and
Fig. 2 Dehydrogenation of SBAB/AB mixture using 1 mol% catalyst
at 60 1C.
c
This journal is The Royal Society of Chemistry 2011
Chem. Commun., 2011, 47, 2922–2924 2923