Communications
To obtain a proof-of-principle for the catalytic homocou-
platinum on charcoal and platinum on alumina afforded
TONs of 190 and 220, respectively. Reducing the catalyst
loading even further to only 0.006 mol%, we showed that the
TON can be again significantly increased, giving a TON of
350 (based on isolated 1).
pling, HBCat and HBPin were combined with various late
transition-metal complexes in a variety of solvents. We
detected the diboranes(4) by GC/MS, although at best only
in trace amounts. We reasoned that a higher concentration of
monoborane in the reaction solution may promote the
formation of B2Cat2 and B2Pin2, in accordance with the
observations of Marder et al.[17] This hypothesis was key to the
development of the coupling procedure: conducting the
reactions in neat borane led to a dramatic improvement in
diborane(4) formation (Table 1).
Given the surprising success of the B2Cat2 synthesis, we
sought to apply this catalytic dehydrocoupling method to
pinacolborane (HBPin). However, this reaction is much less
straightforward than the synthesis of B2Cat2, especially under
homogeneous catalysis conditions. The aforementioned cata-
lysts suitable for the formation of B2Cat2 afforded TONs of no
more than 10 in the case of B2Pin2. Furthermore, the
formation of the latter is accompanied by various side
products, of which PinBOH and (PinB)2O were identified
by mass spectrometry and NMR spectroscopy.[20] Neverthe-
less, we managed to synthesize B2Pin2 under heterogeneous
catalytic conditions using palladium on charcoal and platinum
on charcoal (0.025 mol%), both catalysts affording TONs of
60. As in the case of 1, the output of 2 could be improved by
further reducing the catalyst loading. In the reaction of HBpin
with 0.005 mol% of platinum on alumina, a TON of 93 (based
on isolated 2) was achieved after 8 h.
Table 1: Synthesis of B2Cat2 using homogeneous catalysts.[a]
Entry
Catalyst (loading [mol%])
TON
1
2
3
4
5
6
7
8
[(dppm)PtCl2] (0.05%)
[(dcpe)PtCl2] (0.05%)
[(dcpe)PdCl2] (0.05%)
[(dcpe)NiCl2] (0.05%)
[(dppm)PtCl2] (0.025%)
[(dcpe)PtCl2] (0.025%)
[(dcpe)PdCl2] (0.025%)
[(dcpe)NiCl2] (0.025%)
90
65
75
35
160
90
90
50
For the dehydrocoupling reactions described herein, the
reaction temperature must be chosen carefully. In general,
formation of the diboranes(4) can be observed at temper-
atures as low as 758C, but higher temperatures enhance their
formation significantly. However, boranes such as HBCat are
known to decompose under prolonged heating,[12a] and HBPin
is no exception. Our experiments showed that the best results
could be achieved at temperatures between 1058C and 1108C,
which is only marginally below the boiling points of HBCat
and HBPin. Although the rate of the dehydrocoupling
decreases as the reaction progresses, the yield of diborane(4)
can still be increased slightly by prolonged heating. However,
reaction times exceeding 24 h are best avoided, as degrada-
tion of HBCat and HBPin increases and starts to predominate
over the formation of B2Cat2 and B2Pin2.
[a] Reaction conditions: neat borane is heated with the catalyst to 1108C
for 20 h.
Initially, synthesis of B2Cat2 was attempted under homo-
geneous catalytic conditions. When employing a typical
catalyst loading of 0.05 mol% (Table 1, entries 1–4),
[(dppm)PtCl2]
(dppm = bis(diphenylphosphino)methane)
appears to be the most efficient catalyst, yielding a turnover
number (TON) of 90. With [(dcpe)PdCl2] (dcpe = bis(dicy-
clohexylphosphino)ethane) and [(dcpe)PtCl2], slightly lower
TONs of 75 and 65 were observed. A larger excess of HBCat
(0.025 mol% of catalyst; Table 1, entries 5–8) significantly
improved the TONs to a maximum of 160 for [(dppm)PtCl2].
The next logical step was to investigate the reactivity of
HBCat with common heterogeneous catalysts. When using
0.05 mol% of catalyst (Table 2, entries 1–3), the best results
were achieved with platinum on charcoal (10 wt%) and
platinum on alumina (0.5 wt%), affording 105 and 95 turn-
overs, respectively. In contrast to the homogeneous catalysts,
palladium appears to be far less efficient than platinum, as
palladium on charcoal (10 wt%) yielded a TON of only 35.
Again, by decreasing the catalyst loading, the formation of
B2Cat2 was improved significantly (Table 2, entries 4–6), since
Complete conversion of borane to diborane(4) was not
observed, however. Although strong evolution of hydrogen
occurs initially, a significant decrease is apparent after several
hours. Investigation by GC-MS showed that the rate of
formation of 1 and 2 decreases with increasing reaction time,
and the overall yield does not exceed 5%.
Therefore, we carried out additional experiments to
establish the reason for the decreasing rate of formation of
diboranes(4). The most apparent reason, that is, deactivation
of the catalyst, could be ruled out, as reactions of used
heterogeneous catalyst with fresh borane resulted in almost
identical TONs. Given that a large excess of borane yielded
the best results to date, we reasoned that an increasing
concentration of diborane(4) accumulating in the reaction
mixture might inhibit the reaction. In this case, continuous
removal of the diboranes 1 and 2 from the reaction mixture
should drive the dehydrocoupling forward. We achieved this
by using a Soxhlet-type reaction vessel, in which freshly
distilled, neat borane is continuously reacted with the hot
heterogeneous catalyst, whereas 1 and 2 are purged out of the
reaction zone immediately after their formation (for details
and experimental setup, see the Supporting Information).
Table 2: Synthesis of B2Cat2 using heterogeneous catalysts.[a]
Entry
Catalyst (loading [mol%])
TON
1
2
3
4
5
6
7
Pd on charcoal (0.05%)
Pt on charcoal (0.05%)
Pt on alumina (0.05%)
Pd on charcoal (0.025%)
Pt on charcoal (0.025%)
Pt on alumina (0.025%)
Pt on alumina (0.006%)
35
105
95
75
190
220
350
[a] Reaction conditions: neat borane is heated with the catalyst to 1108C
for 20 h.
ꢀ 2011 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Angew. Chem. Int. Ed. 2011, 50, 12613 –12616