COMMUNICATION
ported to be nearly unreactive with [RuCl
(binap)
E
an induction period and contrasting rate profile with the tri-
methylated catalyst is good evidence that the catalyst is not
converted into another species (i.e., demethylation), al-
though this remains a very unlikely possibility until a cata-
lytic intermediate is isolated. The fastest reactions are limit-
ed, most likely by several factors including an event involv-
ing the ketone substrate (most likely either ketone binding
or nucleophilic attack of hydride), whereas the slower cata-
lyst is slow due to other steps in the catalytic cycle, most
likely hydrogen activation, being retarded to a greater
degree when the NH is not present.
(BINAP = 2,2’-bis(diphenylphosphino)-1,1’-binaphthyl) cat-
alysts (6% yield),[1c] but can be reduced readily with catalyst
4 at room temperature, or more conveniently for kinetic
studies at 708C. A catalyst that can reduce this ketone in
high yield therefore has significant competence in ketone
hydrogenation. We were intrigued to find in batch experi-
ments that all the catalysts reduced a,a-dimethylpropiophe-
none in high yield after 16 h reaction time. Reactions car-
ried out with real-time gas-uptake and subsequent process-
ing of the data in graphical form[5] enable a number of in-
sights to be gained. For brevity, the kinetics graphs are
placed in the Supporting Information. Plotting a graph of
rate against time clearly shows a significant induction time;
maximum turnover frequencies and average initial turnover
frequencies during the first 35 min for all four catalysts are
shown in Table 1, along with notes on the rate profile.
There is a drop in activity and an increase in induction
time in going from catalyst 4 to the achiral P^NH^NH2 cat-
alyst, 5. This indicates that the shape of the catalyst, and
perhaps the geometry at the Ru centre has a very significant
influence on the catalyst productivity. Surprisingly, exchang-
ing the NH2 groups for an NMe2 group as in 6 gives a cata-
lyst with quite similar activity, casting significant doubt on
the primary amine-assisted transition state that would have
seemed likely with these catalysts. There is a significant
drop in activity in switching to the P^NMe^NMe2 catalyst,
7, although this catalyst does slowly reduce a,a-dimethylpro-
piophenone through to completion in about 12 h. The fact
that even trimethylated, 7 does function as a catalyst for this
low reactivity substrate suggests that an inner-sphere mecha-
nism can operate, albeit rather slowly. Both the P^NH^NH2
catalysts 4 and 5 catalyse reduction with pseudo first-order
dependence in ketone concentration. The P^NH^NMe2 cat-
alyst, 6 clearly undergoes a relatively sudden drop in activity
during reaction, although is of broadly similar rate as the
catalyst 5. Most interestingly, the P^NMe^NMe2 catalyst re-
duces this low reactivity ketone with no dependence on
ketone concentration. This was also checked in individual
batch experiments at different concentrations. The lack of
With these results in hand, we were intrigued if similar re-
activity patterns would be present in Noyori catalysts; the
details of these hydrogenations has generated intense inter-
est,[6,7] because of their significant importance. However, de-
spite the quality and depth of the studies reported, the rela-
tive importance of the NH effect to each step in the catalyt-
ic cycle has been rather problematic to study experimentally
since the hydrogenation is fast, and the NH substituents un-
dergo exchange in the protic solvents which are required for
effective catalysis. Noyori reported early on that at least one
primary NH2 group is necessary for effective reaction.[1d]
However, some ketone reduction catalysts that do not have
NH ligands have been reported. We carried out hydrogena-
tions with the “non-NH” catalyst [RuCl2ACTHNUTRGNEUNG
(binap)Py2][8] at dif-
ferent concentrations of acetophenone. These results reveal
that the reactions are also pseudo-zero order in ketone, in
contrast to the pseudo first order kinetics that have been de-
scribed for [RuCl2ACTHNUGTRENNUG(binap)ACHUTNGTREN(NNGU dpen)] (dpen = 1,2-diphenylethy-
lenediamine) under similar conditions (Scheme 2).[6] Thus
ketone binding or reduction is not rate-determining in the
slower hydrogenations catalysed by the non-NH containing
catalyst [RuCl2ACHTNUTRGENNUG(binap)Py2] either.
We were interested to investigate if the presence of NH
groups had any effect on the hydrogenation of alkenes. We
carried out hydrogenation of styrene, a substrate that can be
assumed to be reduced exclusively by inner-sphere process-
es. In our original studies, we found that catalyst 4 does
show significant chemoselectivity for reduction of C=O over
C=C bonds, but it is less chemoselective than Noyori cata-
lysts unless conditions are care-
fully controlled. Thus at 708C,
styrene is hydrogenated within
12 h with all the catalysts with
similar rates for each catalyst
and no significant induction
period. These results argue for
the NH effect (and the sensitiv-
ity to ligand shape) being spe-
cific for ketone hydrogenation;
our view is that the most likely
possibility is that alkene hydro-
genations share very little of
the ketone hydrogenation cata-
lytic cycle, with the cycle oper-
ating being relatively insensitive
to ligand structure.
Table 1. Summary of kinetic data for the hydrogenation of a,a-dimethylpropiophenone using Ru catalysts 4–
7.
Catalyst[a]
Maximum
TOF[b]
Average
Notes on kinetics[c]
initial TOF[b]
4
5
6
7
655
653
403
188
350
106
115
35
induction period followed by pseudo-first-order kinetics
longer induction period followed by pseudo-first-order kinetics
Induction period, then fast reaction with sudden decrease in rate
constant rate throughout; zero order in ketone substrate
[a] Reaction carried out as described in the Scheme and in the Supporting Information, at constant pressure of
70 bar with hydrogen feed monitored. [b] Average initial TOF in mol product per mol catalyst per h measured
from first 35 min of the reaction. Maximum TOF in mol product per mol catalyst per h is the rate reached
after the induction period take from a plot of rate against time.
Chem. Eur. J. 2010, 16, 8002 – 8005
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8003