N. V. Belkova, D. Gelman et al.
Figure 2. Energy profile for the Ir-catalyzed hydroformylation.
Scheme 5. Catalytic labeling experiment: hydroformylation of styrene by
deuterated 1.
mechanism that operates via monohydride intermediates
only.[22]
ysis showed about 60% isotope enrichment at the formyl
group (Scheme 5), proving that the ligand–metal cooperat-
ing mechanism is operative also under catalytic condi-
tions.[19]
Importantly, P NMR analysis of the reaction mixture indi-
cated the presence of a major organometallic species, which
was isolated and crystallographically identified as a new alk-
DFT/M06 calculations were performed to strengthen the
feasibility of the proposed catalytic cycle using 1 (complex
b in Scheme 3) as a catalyst and ethylene as a model sub-
strate (Figure 2; for more details see the Supporting Infor-
mation). Complex b, featuring a pseudo-octahedral geome-
try with a coordinated sidearm and a P-Ir-P angle of about
1008 (fac-arrangement of P-C-P ligand), is taken as the zero-
À
A
energy point. Ethylene insertion into the Ir H bond (b to c)
molecular nucleophilic attack of the hydroxyl sidearm onto
a terminal CO ligand. This complex is a resting state of the
catalyst, since it was found to be equally reactive upon load-
ing it to the reaction in isolated form. The complex may
have relevance in the field of carbon monoxide reduction
and will be studied in details.
turns out to be favorable (DEbÀc =À23.1, DGbÀc =À6.7 kcal
molÀ1) and can be assisted by coordination to the hydroxy-
methylene arm. The barrier to promote proton transfer and
release of the hydrogenated product is about 9 kcalmolÀ1,
which is still lower in energy than the starting material on
the DE scale. The activation energy for this step (DE°cÀa) is
28.0 kcalmolÀ1 (DG°cÀa =25.2 kcalmolÀ1). An estimation of
the gas-phase Gibbs free energy under standard thermody-
namic conditions (298.15 K, 1 atm) shows that all other
transformations in the hydrogenation cycle are spontaneous.
Moreover, the addition of H2 to a is very exoergic, making
the overall hydrogenation process energetically favorable.
For the hydroformylation, the CO addition to ethyl com-
plex c is very exoergic (Figure 2). CO insertion (d to e) fur-
ther lowers the energy of the system about 6 kcalmolÀ1.
Similar to the hydrogenation cycle, the release of the alde-
hyde product proceeds through proton transfer from a pend-
ant OH group to the carbon of the alkanoyl ligand. This
step is endoergic again, however, it is more energy demand-
ing (by ca. 20 kcalmolÀ1) than in the case of hydrogenation.
This is in agreement with the more rigorous conditions that
are necessary for hydroformylation to occur.
Scope and limitations studies showed that the chemo- and
regioselectivity of catalyst 1 in hydroformylation reactions
(Table 1, entries 1–5), for which hydrogenation is a very
competitive process,[20] is largely comparable with the state-
of-the-art iridium-based catalysts. However, rhodium-based
catalysts showed a higher chemoselectivity in the hydrofor-
mylation of olefins. Thus, in the presence of 3, essentially no
hydrogenation product was observed, even under 14 bar of
1:1 syngas (Table 1, entries 6–14). For example, nonisomeriz-
able substrates, such as differently substituted styrenes and
2-vinyl naphthalene (Table 1, entries 6–11), were successfully
hydroformylated to a mixture of the branched and linear al-
dehydes. Hydrogenation was also not observed in the Rh-
catalyzed hydroformylation of isomerizable alkenes
(Table 1, entries 12–14). In these cases, isomerization can
precede hydroformylation, but all double-bond regioisomers
eventually react. Thus, both 1-octene and trans-2-octene led
to the formation of 1-nonanal, 2-methyloctanal and 2-ethyl-
heptanal in comparable ratios. The highest TON of 727
demonstrated by 3 was obtained in the hydroformylation of
styrene.
In conclusion, we have described a conceptually new
mechanism for the hydroformylation of olefins. The mecha-
À
nism for the H2 activation and C H bond formation in-
volves an intramolecular cooperation between the structur-
ally remote functionality and the metal center. This is the
most important aspect of our work, because coordinational
diversity in ligand–metal cooperating catalytic systems
offers new reaction patterns in many classical reaction
schemes and renders new reactivity to many classical or-
It is worth noting that a fast isomerization is not charac-
teristic for the conventional rhodium-catalyzed hydroformy-
lation, because rhodium–phosphine–dihydride species show
very little, if any, tendency toward olefin isomerization.[21]
This observation again supports the proposed cooperative
ACHUTNGERNgNUG anoHCATUNGTRENNmUGN etallic compounds. Further synthetic and catalytic
16908
ꢂ 2013 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Chem. Eur. J. 2013, 19, 16906 – 16909