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a precatalyst for the hydrogenation of cyclohexyl hexanoate.
To our delight, under similar reaction conditions used for the
precatalyst 1, 2 gave 85% yield of cyclohexanol with the
formation of 79% hexanol (Table 1, entry 2). The complex 3,
under the same reaction conditions, gave a lower yield (67%)
of cyclohexanol (entry 3). Increasing the loading of 2 to
4 mol% and the reaction time to 65 hours did not result in
significantly higher yield of cyclohexanol (88%; entry 4).
Activation of the 2 with only 1 equivalent of NaHBEt3 gave
a lower yield of cyclohexanol under similar hydrogenation
conditions (entry 5). The amount of the base has a significant
effect on the yield of the ester hydrogenation reaction.
Increasing the precatalyst/base ratio to 1:12.5 increased the
yield of cyclohexanol (99%), whereas decreasing the ratio to
1:2 gave only 20% product (entries 7 and 8). Without reacting
the pre-catalyst with NaHBEt3 only a moderate yield (50%)
was obtained even at high precatalyst/base ratio (1:12.5;
entry 9). Decreasing the precatalyst loading to 1 mol% gave
54% yield after 70 hours in the presence of 14 mol% base
(entry 10). Among the different bases, tBuOK was found to
be better than NaOMe, NaOEt, and potassium bis(trimethyl-
silyl)amide (KHMDS), and among the solvents screened,
THF was a better choice than toluene or 1,4-dioxane
(entries 11–15).
Next, the scope of the reaction was examined with various
esters, including primary, secondary, and tertiary aliphatic
esters. Thus, 1 mmol of cyclohexyl hexanoate under 50 bar
pressure of H2 at 1308C in THF, in the presence of 2 (2 mol%)
gave 85% yield of cyclohexanol and 79% yield of hexanol
after 38 hours (Table 2, entry 1). A small amount of hexyl
hexanoate was also observed as a result of the transesterifi-
cation reaction between the formed hexanol and cyclohexyl
hexanoate. Under similar reaction conditions, hexyl hexa-
noate gave 67% yield of hexanol after 43 hours. By increasing
the precatalyst loading to 4 mol%, the yield of hexanol
increased to 87% (entry 2). Similarly, pentyl pentanoate gave
67 and 85% pentanol by using 2 and 4 mol% precatalyst,
respectively (entry 3). Under similar reaction conditions,
other aliphatic esters also gave good yields of the hydro-
genated product. g-Valerolactone gave a moderate yield
(50%) of 1,4-pentanediol (entry 11).
Aliphatic esters are normally considered to be more
challenging substrates for catalytic hydrogenation than aro-
matic ones because of the generally higher electophilicity of
the carbonyl carbon atom in the latter, thus making hydride
transfer to the carbonyl group of aromatic esters more facile.
Very surprisingly, this was not the case in the reactions
reported here. Thus, methyl benzoate was not hydrogenated
at all under similar reaction conditions. (Table 2, entry 12).
Also, 2,2,2-trifluoroethyl trifluoroacetate, which is expected
to be even more activated towards hydride transfer to the
carbonyl group, remained unreacted (entry 13). In light of this
unexpected inverse reactivity in the hydrogenation reaction
we envisioned that the hydrogenation reaction might proceed
by the enolate form of the ester, which is in equilibrium with
the ester under the basic reaction conditions, and hence non-
enolizable esters do not react. Mechanistically, the enolate
can undergo hydrogenation to generate the salt of a hemi-
acetal intermediate which can form an aldehyde and alkoxide,
Figure 2. a) Molecular structure of 2 with thermal ellipsoids set at
50% probability. Hydrogens except H2 on the amine were omitted for
clarity.[21] Selected bond lengths [ꢀ] and angles [8]: Co1–N1 2.0902(13),
Co1–N2 2.2679(12) Co1–Cl2 2.2938(5), Co1–Cl1 2.3027(5), Co1–P1
2.4938(4), N2–H2 0.85(2); N1-Co1-N2 76.71(5), N1-Co1-Cl2 128.81(4),
N2-Co1-Cl2 97.28(4), N1-Co1-Cl1 104.02(4), N2-Co1-Cl1 89.38(4), Cl2-
Co1-Cl1 126.934(17), N1-Co1-P1 79.83(4), N2-Co1-P1 156.49(3),
Cl2-Co1-P1 96.295(16), Cl1-Co1-P1 97.656(16). b) Molecular structure
of 3 with thermal ellipsoids set at 50% probability. Hydrogens were
omitted for clarity. Selected bond lengths [ꢀ] and angles [8]: Co1–N1
2.1783(11), Co1–N2 2.2430(12), Co1–Cl2 2.3081(4), Co1–Cl1
2.3244(4), Co1–P1 2.4724(4); N1-Co1-N2 75.88(4), N1-Co1-Cl2
160.77(3), N2-Co1-Cl2 97.72(3), N1-Co1-Cl1 95.99(3), N2-Co1-Cl1
97.71(3), Cl2-Co1-Cl1 102.877(14), N1-Co1-P1 78.04(3), N2-Co1-P1
142.37(3), Cl2-Co1-P1 98.075(14), Cl1-Co1-P1 111.639(14).
cyclohexyl hexanoate under 50 bar H2 pressure at 1308C in
THF in the presence of 25 mol% tBuOK. Only 27% yield of
cyclohexanol and 11% yield of 1-hexanol were obtained after
38 hours (Table 1, entry 1).
Table 1: Optimization of the reaction conditions for cobalt-catalyzed
hydrogenation of esters.[a]
Entry Precatalyst NaHBEt3 Base
t [h] Solvent Base
Yield
[%][b]
(mol%)
(mol%) (mol%)
1
2
3
4
5
6
7
8
9
1 (2)
2 (2)
3 (2)
2 (4)
2 (2)
2 (4)
2 (4)
2 (4)
2 (4)
2 (1)
2 (2)
2 (2)
4
4
4
8
2
8
8
8
–
2
4
4
25
25
25
25
25
16
50
8
50
14
25
25
38 THF
38 THF
38 THF
65 THF
38 THF
65 THF
48 THF
65 THF
48 THF
72 THF
tBuOK
27
85
67
88
65
70
99
20
50
54
41
32
tBuOK
tBuOK
tBuOK
tBuOK
tBuOK
tBuOK
tBuOK
tBuOK
tBuOK
10
11
12
38 toluene tBuOK
38 1,4- tBuOK
dioxane
13
14
15
2 (2)
2 (2)
2 (2)
4
4
4
25
25
25
38 THF
38 THF
38 THF
KHMDS 38
NaOMe 28
NaOEt
32
[a] Reaction conditions: ester (1.0 mmol), THF (1 mL), H2 (50 bar),
1308C. [b] Determined by GC with respect to cyclohexanol. THF=te-
trahydrofuran.
Recently, we developed a pyridine-based PNNH/Ru
complex with the potential for dual-mode metal–ligand
cooperation, and it catalyzes the hydrogenation of esters at
room temperature and low pressure.[17] Following this obser-
vation, the PNNH-based cobalt complex 2 was studied as
2
ꢀ 2015 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Angew. Chem. Int. Ed. 2015, 54, 1 – 5
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