Angewandte
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moieties, in line with the bonds leading to the naphthalene
(Figures 1d,e).
the presence of Leonard turns (Figure 2a and Table 1,
entries 5–8).
Control compound 13, with a loose tetramethylene turn,
In view of these considerations, we were delighted to find
that under routine conditions at 208C,[2] our first Leonard
catalyst 9 catalyzed the addition of MAHT 1a to nitroolefin 2
selectively: The intrinsically disfavored (d) addition product
3a was obtained in hd = 65% yield, with the naturally more
favored (f) decarboxylation product 4a generated in hf = 34%
(Table 1, entry 5). The resulting selectivity, hd/f = 1.9, was
outstanding considering that the original catalyst 23, which
features a loose turn, failed to cause the desired selectivity
inversion (hd/f = 0.8; Figure 2a and Table 1, entry 19). The
new Leonard catalyst 9, as simple as it gets, was already as
good as the most developed original tweezer catalyst 22, with
two NDIs next to the amine and two sulfones in the NDI core
maximizing effective molarity and p acidity, respectively
(Figure 2a and Table 1, entry 18). Increasing selectivity
upon oxidation of the sulfides in the core of 9 to sulfoxides
in 10 and sulfones in 11 (hd/f = 2.5 and 2.8) and the absence of
selectivity inversion with control catalyst 12 without a p sur-
face (hd/f = 0.7) confirmed operational anion–p interactions in
failed to perform as well as Leonard catalyst 9 (Figure 2a).
However, increasing selectivity inversion with increasing
p acidity in 13–15 revealed the existence of “tortoise-and-
hare” anion–p catalysis also with looser turns (Table 1,
entries 9–11). Control compound 16, with a bulky Hünigꢀs
base analogue in the Leonard turn, performed only slightly
better than control 17 without a p surface (hd/f = 0.9 vs. hd/f
=
0.7; Table 1, entry 12 and 13), presumably because the steric
crowding hinders operational anion–p interactions. Increas-
ing the effective molarity of the p surfaces in tweezer-like
Leonard catalysts 18 and 19 did not improve the outstanding
activity of the most simple, most compact monomeric
Leonard catalysts 9–11 (Figure 2a and Table 1, entries 14
and 15 vs. 5–7).
In catalyst 5, the flexible Leonard turn of catalyst 9 is
rigidified (see TS2 in Figure 1e). In doing so, the selectivity
inversion increased to hd/f = 3.1 (Table 1, entry 1). Increasing
the p acidity in catalysts 6 and 7 further improved the activity
to hd/f = 3.8 and hd/f = 4.4 (Table 1, entries 2 and 3).
The hd/f = 0.9 value for control 8 without a p surface
Table 1: Characteristics of the anion–p catalysts and control compounds.[a]
confirmed that these quite spectacular results orig-
Cat.[b] p Acidity[c] Substrate[d] hd
[%][e]
hf
[%][f]
hd/f[g]
DDGTS
°
inate from maximizing the anion–p interactions with
the rigidified Leonard turn in catalysts 5–7. Com-
parisons over the full series of comparable architec-
tures, from original and loose turns in 23 (hd/f = 0.8)
and 13 (hd/f = 1.1) to flexible Leonard turns in 9
(hd/f = 1.9), beautifully illustrate the unique power of
fixed Leonard turns in 5 (hd/f = 3.1) to run reactions
on p surfaces and maximize contributions from
anion–p interactions for catalysis (Figure 2a). The
same trend holds true at maximal p acidity, moving
from hd/f = 2.3 for loose turns in 15 to hd/f = 2.8 with
flexible Leonard turns in 9 and hd/f = 4.4 with fixed
Leonard turns in 7.
[kJmolÀ1 [h]
]
1
2
3
4
5
6
7
8
9
5
6
7
8
+
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1a
1b
1b
1b
1b
1b
1b
84 (74) 12 (24)
87 (77) 11 (20)
7.0 (3.1) À3.6 (À3.0)
7.9 (3.8) À3.9 (À3.5)
9.6 (4.4) À4.3 (À3.9)
+ +
+ + +
À
86 (80)
9 (18)
57 (47) 39 (52)
78 (65) 19 (34)
80 (68) 15 (27)
84 (74) 13 (26)
59 (43) 40 (56)
70 (50) 28 (47)
81 (64) 19 (32)
83 (68) 16 (30)
73 (43) 25 (48)
1.5 (0.9)
–
9
+
4.1 (1.9) À2.3 (À2.3)
5.3 (2.5) À2.9 (À2.9)
6.5 (2.8) À3.4 (À3.4)
10
11
12
13
+ +
+ + +
À
1.5 (0.7)
–
+
2.5 (1.1) À1.2 (À1.1)
4.3 (2.0) À2.4 (À2.6)
5.2 (2.3) À2.9 (À2.9)
2.9 (0.9) À1.5 (À0.6)
10 14
11 15
12 16
13 17
14 18
15 19
16 20
17 21
18 22
19 23
20 24
21
22
23
24 10
25 11
26 12
+ +
+ + +
+
À
(40)
87 (51) 12 (23)
89 (54)
(54)
(0.7)
–
Reactions run at 78C instead of 208C gave the
same overall trends (Figure 2b). For example, the
steady increase from original and loose turns in 23
(hd/f = 2.3) and 13 (hd/f = 2.5) to flexible Leonard
turns in 9 (hd/f = 4.1) and fixed Leonard turns in 5
(hd/f = 7.0) remained intact (Figure 2a). The overall
higher selectivity is consistent with the notion of
strengthened anion–p interactions at lower temper-
atures. In this instance, the impact of flexible as well
as fixed Leonard turns was less pronounced, whereas
the effective molarity of the p surfaces became more
important. For example, loose tweezers 22 at max-
imal p acidity reached the selectivity of fixed
Leonard turns 5 at minimal p acidity (Figure 2b);
at 208C, 22 was clearly less active than 5 (Figure 2a).
Moreover, the overall best performance was found
for tweezers 19 with flexible Leonard turns and
intermediate p acidity (hd/f = 11.1), although the
fixed Leonard turns in monomeric 7 were almost
as good (hd/f = 9.3, Figure 2b); at 208C, 19 was much
less selective than 7 and also 5 (Figure 2a). This
overall reduced importance at lower temperature
+
7.3 (2.0) À3.7 (À2.6)
+ +
+
+ +
+ + +
+
8 (27) 11.1 (2.2) À4.6 (À3.4)
71 (50) 23 (48)
80 (59) 14 (36)
80 (59) 11 (31)
69 (46) 30 (54)
60 (37) 30 (53)
3.1 (1.0) À1.2 (À0.9)
5.7 (1.6) À2.9 (À2.0)
7.3 (1.9) À3.5 (À2.6)
2.3 (0.8) À0.7 (À0.8)
À
2.0 (0.7)
1.9
3.0
1.4
1.9
–
5
7
9
+
65
74
59
64
68
42
34
25
41
33
32
57
À2.3
À3.4
À1.6
À2.3
À2.6
–
+ + +
+
+ +
+ + +
À
2.1
0.7
[a] Reactions were conducted in [D8]THF with 20 mol% of the catalyst and
monitored by 1H NMR spectroscopy. [b] Catalysts, see Figure 2 for their structures.
[c] Qualitative indication of the p acidity, À=no p surface. [d] Substrates; 1a:
200 mm with 2m 2; 1b: 200 mm with 1.5m 2. [e] Yield of the intrinsically disfavored
products 3a/3b in THF at 78C (in parentheses: hd at 208C). [f] Yield of the
intrinsically favored products 4a/4b at 78C (208C). [g] Selectivity hd/f =hd/hf at 78C
(208C). [h] Selective catalysis: The difference in the Gibbs free energies
DGTS° (catalyst) of the two transition states leading to the intrinsically favored (f)
and disfavored (d) products, calibrated against the nearest control DGTS° (8, 12, 17,
24); DGTS° =ÀRTln(hd/f),[16] DDGTS° =DGTS° (catalyst)ÀDGTS° (control). Data for
20–24 are from Ref. [2].
Angew. Chem. Int. Ed. 2016, 55, 4275 –4279
ꢀ 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
4277