Angewandte
Chemie
Table 1: Screening results of reaction conditions.[a]
Recently, organocatalytic asymmetric transfer hydroge-
nation with organic hydride donors[11] has emerged as
a powerful method for the construction of diverse cyclic and
acyclic amines by reduction of imines in the presence of
Brønsted acids. Based on the “three-point contact model” for
asymmetric transfer hydrogenation reported recently by
Goodman and co-workers,[12] we envisioned that an organo-
catalytic kinetic resolution through a phosphoric acid cata-
lyzed[13] imine formation and transfer hydrogenation cascade
process could potentially be a powerful and general approach
toward chiral BINAM derivatives. This strategy consists of
consecutive asymmetric kinetic resolution process by means
of chiral phosphoric acid catalysis, in which installing a bulky
group in one of amines of racemic BINAM was presumed to
increase the rotation energy barrier and effective steric
interaction for improved enantioselectivity (Scheme 1b).
Herein, we present the details of our studies with this strategy.
To validate the feasibility of the proposed process, we
selected N-[2’-amino(1,1’-binaphthalen)-2-yl]naphthalene-2-
sulfonamide rac-1a with a bulky naphthalenesulfonamide
group as the model substrate for the optimization of reaction
conditions. We initiated our studies by evaluating the reaction
between rac-1a and 0.6 equiv of 2-naphthaldehyde 2a using
10 mol% of chiral phosphoric acid 4a as the Brønsted acid
catalyst and diethyl 2,6-dimethyl-1,4-dihydropyridine-3,5-
dicarboxylate (HEH1) as the hydride source in ethyl acetate
(EA) at room temperature for 48 h. To our delight, the
reaction proceeded smoothly and afforded the desired
product 3a in 43% yield with 93% ee, albeit with only
moderate ee (53%) of the recovered starting material (R)-
1a[14] (Table 1, entry 1). After calculation, a selectivity fac-
tor[9a] (S = kfast/kslow) of 47 was obtained (entry 1). Encouraged
by this, a detailed optimization study was first done with
different phosphoric acid catalysts. Several BINOL, H8-
BINOL, SPINOL, and VAPOL-derived catalysts were inves-
tigated, which displayed remarkable effects on the outcome of
the reaction. It should be noted that the yield and ee of
product 3a was always excellent with different BINOL-
derived catalysts (Table 1, entries 2–6), even in the presence
of the catalyst with phenyl group on the 3,3’-positions
(Table 1, entry 3), while ee of the recovered 1a varied. It is
interesting to find that the kinetic resolution reaction did not
proceed with VAPOL 4i as catalyst, which is most likely due
to the steric hindrance with the bulky starting material
(Table 1, entry 9). Considering catalyst 4e with the best
results (S = 354) for both the transfer hydrogenation product
3a (50% yield, 98% ee) and the recovered starting material
(R)-1a (41% yield, 94% ee) (Table 1, entry 5), this catalyst
was selected for further optimization. Predictably, the solvent
played an important role in this transformation, especially as
to the enantioselectivity of the recovered starting material,
and EA was proved to be the best choice (Table 1, entries 10–
14). Inspired by a recent review on Hantzsch esters as the
hydride sources for transfer hydrogenations,[16] we screened
different Hantzsch esters (Table 1, entries 15–17) and found
that HEH3 gave rise to a better result (S = 303) with 98% ee
of the recovered 1a and 97% ee of the product (Table 1,
entry 16). Finally, we investigated the effects of the reaction
Entry cat. HEH Solvent
3a
1a
S[d]
yield
[%][b]
ee
yield
ee
[%][c] [%][b]
[%][c]
1
2
3
4
5
6
7
8
4a
4b
4c
4d
4e
4 f
4g
4h
4i
4e
4e
4e
4e
4e
4e
4e
4e
1
1
1
1
1
1
1
1
1
1
1
1
1
1
2
3
4
3
3
3
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc NR
DCE 27
toluene 40
MTBE 36
43
48
42
52
50
44
42
46
93
94
98
95
98
50
46
49
37
41
46
50
45
53
73
47
71
87 283
48 63
94 354
83 259
98
À97
À74 146
98
88 290
9
ND NR
ND
24
73
75
38
–
8
42
48
28
10
11
12
13
14
15
16
17
73
90
91
90
98
98
97
99
98
98
97
69
39
44
50
49
47
44
43
46
44
46
CH3CN 25
iPrOAc 41
86 276
80 244
98 303
97 844
92 328
64 192
99 327
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc
EtOAc
48
47
45
50
46
47
18[e] 4e
19[f] 4e
20[g] 4e
[a] Reaction conditions: rac-1a (0.050 mmol), Hantzsch ester
(0.70 equiv), catalyst 4 (10 mol%), EtOAc (0.6 mL). [b] Determined by
chiral stationary phase HPLC analysis. [c] Yield of isolated product.
[d] The selectivity factor was calculated as S=ln[(1ÀC)(1Àee(1a))]/
ln[(1ÀC)(1+ee(1a))], C=ee(1a)/(ee(3a)+ee(1a)). [e] 10 mg of 3 ꢀ MS
was added. [f] The reaction was run at 508C. [g] The reaction was
performed at 108C for 72 h.
temperature and 3 ꢁ molecular sieves as the additive without
significant improvement (Table 1, entries 18–20).
With the optimal reaction conditions in hand, we set out to
explore the substrate generality of this procedure. As shown
in Table 2, the functional groups on aldehydes, such as 1-
naphthyl, 2- naphthyl, 6-OMe-2-naphthyl, and 4-chlorobenzyl
groups, were well-tolerated, giving the corresponding prod-
ucts 3a-3d in good to excellent enantioselectivities with good
yields (S = 15–303, Table 2, entries 1–4). Notably, the 2-
naphthaldehyde exhibited the best performance in terms of
stereoselectivity and yield for both of the product 3a and
recovered starting material 1a, indicating an aromatic stack-
ing interaction during the transfer hydrogenation step.
Based on this observation, we next examined other bulky
protecting groups for this process. This reaction shows
excellent compatibility with different types of protecting
groups, such as sulfonyl, benzoyl, 2-naphthylmethyl, Fmoc,
amido and thioamido groups (S = 7-340, Table 2, entries 5–
Angew. Chem. Int. Ed. 2014, 53, 3684 –3687
ꢀ 2014 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
3685