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novel catalytic systems that allow the hydrogenation of nitriles
to be performed under mild conditions, without additives,
while providing a high selectivity in the desired amines.
catalyst BH4-7,[46] in which the Cl ligand was replaced by BH4
,
was used with no added base.[47]
Indeed, compound 11 was quantitatively hydrogenated over
3 h under base-free conditions with 1 mol% of BH4-7 at 708C
and 30 bar of hydrogen (Table 4, entry 1). To our delight, the
reaction proceeded smoothly, even at lower catalyst loadings
(Table 4, entries 2–5), reaching a TON of about 2000 at
0.05 mol%; this is the highest TON reported so far for this reac-
tion. When either the catalyst loading (Table 4, entry 6) or the
hydrogen pressure were reduced further (Table 4, entry 7), the
reaction became slower thus favoring the formation of the sec-
ondary imine in moderate yields.
To assess the catalytic activity of the novel complexes in ni-
trile hydrogenation, benzonitrile (11) was chosen as a standard
substrate (Figure 6 and Table S1 in the Supporting Informa-
tion). To begin with, reactions were carried out for 3 h in iPrOH
at 708C under 30 bar of hydrogen with 1 mol% of the catalyst
Quantitative yields of 12 were obtained, even at 508C, when
using 0.1 mol% BH4-7 (Table 4, entry 9). By comparing the re-
sults in entries 9 and 11 in Table 4 (reaction times of 3 and 1 h,
respectively, under otherwise identical conditions), it is evident
that in the initial stages of the reaction the main product is
the secondary imine, which, through the equilibria described
in Scheme 6, reverts back to the primary imine as the reaction
proceeds and is eventually hydrogenated to the primary
amine.[33b]
A few solvents, other than iPrOH, were screened (Table S3 in
the Supporting Information): complex BH4-7 was only active in
THF; however, the yield of 12 was quite low. The reaction did
not proceed in the absence of hydrogen (Table 4, entry 8). Sim-
ilar experiments were carried out to study the influence of cat-
alyst loading, pressure, and temperature on the reduction of
13 in the presence of BH4-7 (Table 5). As for 11, the screening
results show that for better selectivity the three parameters
have to be adjusted to secure a fast enough reaction to pre-
vent the intermediate imine from reacting with the product
amine (Table 5, entries 3 and 6). The best compromise was ob-
tained when using 0.5 mol% of catalyst at 708C under 15 bar
of H2, affording heptylamine (14) in excellent yield (98%;
Table 5, entry 4) over 3 h. Even in this case, no reaction took
place in the absence of hydrogen (Table 5, entry 5).
Figure 6. Comparison of the catalytic activity of complexes 3–10 in the hy-
drogenation of 11 to afford 12 in 30 bar hydrogen.
and a minimum amount of base (5 mol% of KOtBu). Under
these conditions, all catalysts afforded quantitative yields of
benzylamine (12), with the exception of 8 and 10, which gave
the product in moderate to low yield (Table S1, entries 1–8, in
the Supporting Information). To probe the influence of base,
the best performing catalysts were tested with the amount of
base strictly necessary to generate the catalytic active species
by their dehydrochlorination: one equivalent to ruthenium for
3–7; two for 9, under otherwise identical conditions.[45] Indeed
complexes 4, 5, 6, and 7 catalyzed the formation of 12 in ex-
cellent yields, whereas 3 and 9 showed a lower activity and se-
lectivity, which resulted in the preferential formation of the
secondary imine S1 (Table S1, entries 9–14, in the Supporting
Information). At a lower catalyst loading (0.5 mol%), only com-
plexes 5–7 were active enough to secure the quantitative and
selective formation of 12 over the 3 h of reaction time
(Table S1, entries 16–18, in the Supporting Information). Cata-
lyst 4 was less efficient and afforded exclusively the secondary
imine S1 (Table S1, entries 15, in the Supporting Information).
Finally, by decreasing the temperature to 508C, it was possible
to identify 7, among the structurally related catalysts 5–7, as
the most active catalyst for the reduction of 11 to 12, which
proceeded in 85% yield (Table S1, entries 19–20, in the Sup-
porting Information). Also, in a similar screening, complex 7
was the most active and selective catalyst for the hydrogena-
tion of the aliphatic nitrile 1-heptanenitrile (13) as well
(Table S2 in the Supporting Information).
Having assessed to which extent reaction conditions might
be mitigated without compromising yield and selectivity, the
general applicability of the new system was evaluated in the
hydrogenation of several aromatic and aliphatic nitriles. Table 6
summarizes the results obtained with aromatic and heteroaro-
matic nitriles. All experiments were carried out under 30 bar of
hydrogen. In most cases, excellent yields of primary amines
were obtained at 508C with 0.5 mol% of BH4-7. Both electron-
donating (Table 6, entries 3–8) and -withdrawing groups
(Table 6, entries 9–12) are tolerated, including ortho-substituted
derivatives.
Benzonitriles with either an ester or an amido group are se-
lectively hydrogenated, too. For methyl 4-cyanobenzoato, se-
lectivity was achieved by shortening the reaction time (Table 6,
entry 13). In case of N-(4-cyanophenyl)acetamide, reduction of
the sole cyano group was achieved at 708C over 3 h.[22] Gratify-
ingly, selected heteroaromatic nitriles were efficiently hydro-
genated to the corresponding amines (Table 6, entries 15–20).
Under mild reaction conditions, 3- and 4-pyridinecarbonitrile,
but not 2-pyridinecarbonitrile, afforded the corresponding pi-
colylamines in high yields (Table 6, entries 15 and 16). The 2-
Notably, catalyst 7 requires only one equivalent of base to
promote the reduction of 11. This means that base might be
needed only in the initial stage of the process to generate the
catalytic active species. Therefore, for subsequent experiments,
Chem. Eur. J. 2016, 22, 4991 – 5002
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