10.1002/chem.201905466
Chemistry - A European Journal
COMMUNICATION
screened including toluene, naphthalene, anthracene, and
styrene (Table 1) (Scheme 3). All reactions were performed
full consumption of the naphthalene. While Rothwell’s niobium
catalysts are capable of hydrogenating tetralin to decalin under
under 150 psi of H2 at 80 °C with ferrocene as an internal standard. 1200 psi of H2,[1b] the same was not observed for Chirik’s
homogeneous molybdenum system, even when increasing the H2
pressure from 59 to 470 psi.[8]
With respect to the hydrogenation of anthracene by 1, its
relative rate is similar to that of naphthalene and selectively forms
1,2,3,4,5,6,7,8-octahydroanthracene (Table 1) (Figures S30 and
S40), though it must be noted that the rate of reaction is severely
limited by the poor solubility of the anthracene under the reaction
conditions.
Surprisingly, there is no indication of the presence of any
monocyclic-hydrogenated 1,2,3,4-tetrahydroanthracene in the
reaction mixture, indicating that it is immediately hydrogenated
upon formation. In comparison, Rothwell’s catalysts give access
to both 1,2,3,4-tetrahydroanthracene and 1,2,3,4,5,6,7,8-
octahydroanthracene
(1200
psi,
80
°C),[1b]
while
perhydroanthracene is the major product of Mutterties’ cobalt
catalyzed reactions.[5a]
Curiously, 1 does not catalyze the aromatic hydrogenation of
styrene to ethylcyclohexane under the general conditions of our
experiments. Instead, it acts as an olefin hydrogenation catalyst
that selectively hydrogenates styrene to ethylbenzene (TON = 9.0,
20 hours) without the formation of ethylcyclohexane (Figures S31
and S41). This transformation takes place at room temperature
and occurs at a higher relative rate than the hydrogenation of
aromatic substrates (Table 1). Upon full consumption of the
styrene, formation of ethylcyclohexane from the hydrogenation of
ethylbenzene is not observed even upon heating the sample at
80 °C over the course of 7 days (Figure S31). Similarly, starting
with ethylbenzene in place of styrene results in no change after
80 h at 80 °C under H2 (150 PSI) (Figure S34). In comparison, (4-
tBu-iPrBDI)Mo(CH2SiMe3)2 also hydrogenates styrene to
ethylbenzene (59 psi), while higher pressures (470 psi) leads to
ethylcyclohexane exclusively.[8] Regardless, when compared
against A, 1 was found to be a superior hydrogenation catalyst as
it gives significantly higher turnovers of ethylbenzene under
comparable conditions (80 °C, 150 psi H2, 18 h, and 8.0 mM in
C6D12), TON = 6 (1) vs TON = 2.5 (A), possibly due to the more
favorable steric profile of 1.
It should be noted that in the case of anthracene and styrene,
the formation of intermediates are observed by 1H NMR
spectroscopy (Figures S30 and S31), which we putatively assign
as the catalytically active species (ImDippN)(Xyketguan)Ti(η6-C12H14)
and (ImDippN)(Xyketguan)Ti(η2-C2H3C6H5), lending credence to the
steps of our proposed catalytic cycle (Scheme 3). In contrast, the
toluene and naphthalene analogs are not seen suggesting these
intermediates are rapidly hydrogenated upon formation.
Finally, attempts to hydrogenate substituted arenes such as
Me3SiPh, phenyl boronic acid pinacol ester, anisole, and aniline
were not met with success, either leading to no observed
reactivity (Me3SiPh) or catalyst decomposition (pinacolborane,
aniline, and anisole). The decomposition of our system by N- and
O-atom containing heterocycles is not surprising as we have
shown our masked Ti-complexes to be potent reductants that are
highly reactive towards heteroatom donors.[13] This suggests that
ligand modifications will be necessary to temper the reactivity to
mitigate such unwanted chemistries.
Scheme 3. Proposed catalytic cycle.
As compared to C6D6, neat toluene-d8 is more rapidly
hydrogenated with nearly twice the TON over the first 20 hours
(Table 1) (Figures S28 and S38). This is surprising, as in the case
of the macrocyclic phosphine amide R[P2N2]Nb(CH2SiMe3), the
catalytic competency of the niobium complex drops precipitously
from benzene to toluene.[7]
Rothwell’s niobium arene
hydrogenation catalysts also show a decrease in relative rate from
benzene to toluene, though, no other correlation between
hydrogenation rates and sterics can be drawn from his system.[1b]
Though, it should be noted, that when using fewer equivalents of
toluene-h8 (20 equiv) in C6D12 with 1, the decrease in the rate of
hydrogenation is pronounced (TON < 0.7 after 20 h) (Figure S33).
The hydrogenation of naphthalene by
1 occurs at a
significantly faster initial rate than the pseudo first order C6D6 or
C7D8 reactions, cleanly producing 1,2,3,4-tetrahydronaphthalene
(i.e., tetralin) (Table 1) (Figures S29 and S39). Consecutive
hydrogenation of tetralin to decalin was not observed even after
Table 1. Catalytic hydrogenation of select unsaturated aromatics.[a]
TON TOF[d]
(20 h)
Total TON[e]
(60 h)
Substrate
Product
(h-1)
0.05
[b]
C6D6
cyclohexane-d6
1.0
2.0
[b]
0.09
0.22
Toluene-d8
Naphthalene
Anthracene
Styrene[c]
methylcyclohexane-d8
1.8
4.4
4.6
9.0
2.9
7.4
tetralin
In closing, we have previously shown that our arene-masked
Ti(II) synthon (A) affords access to novel and distinctive late-metal
type reactivity, namely transfer hydrogenation of cyclic olefins.[11]
Building upon this success through subtle but judicious ligand
octahydroanthracene
0.23
0.45
6.5
13.9[c]
ethylbenzene
Pinacolborane
Me3SiPh
–
–
–
–
modification, we have now reported a new platform, 1intra and 1inter
,
with improved thermal stability. Importantly, the steric profile of
1intra and 1inter allows for the intermolecular capture and activation
of aromatic hydrocarbons at the titanium center, catalyzing the
hydrogenation of monocyclic (benzene and toluene) and
polycyclic (naphthalene and anthracene) arenes under relatively
mild conditions (150 psi, 80 °C). Moreover, our new system also
selectively hydrogenates the olefinic substituent of styrene to give
Anisole
Aniline
[a] Reactions conducted using solutions of 1intra (0.036 mmol,1.0 mL) with 20
equiv of substrate at 80 °C under H2 (150 psi) in C6D12 with Fc (0.0269 mmol)
as internal standard. [b] Substrate as solvent. [c] Room temperature reaction,
60 h. [d] Average turnover frequency over 20 hours. [e] Averaged over three
runs.
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