Table 1. Critical Role of Base in the Indole C2-Arylation
Reactionsa
yield %
Figure 1. Proposed kinetic model of the reaction system.
entry
base
MgO
ZnO
CS2CO3
KOAc
solvent
product
biphenyl
1
2
3
4
5
6
dioxane/DMF (1:2)
dioxane/DMF (1:2)
DMA
3
8
21
27
48
11
12
24
28
34
28
37
then undergo two competing pathways: (1) cross-coupling
with the substrate to furnish the desired product or (2)
formation of byproduct biphenyl. Although the mechanistic
details of these processes have not been elucidated,5 we made
an informed assumption that biphenyl formation required a
bimolecular transmetalation of the aryl-palladium species
(Figure 1).11
DMA
DMA
DMA
CsOAc
CsOTFA
a All yields were determined by HPLC versus an internal standard. For
complete data, see Supporting Information.
Despite its simplicity, this model predicts several features
of significant practical consequence. For instance, decreasing
the catalyst loading should increase the rate ratio V3/V2 and
thus faVor production of the desired product. To test this
hypothesis, arylation of N-methylindole with iodobenzene
was conducted over a range of catalyst loading; in these
experiments, the concentration of the substrate was kept
constant (Figure 2). Indeed, decreasing the amount of catalyst
indoles. A significant improvement was accomplished via a
systematic investigation of the base, which ultimately led
us choose cesium acetate as the optimum reagent (Table 1,
entry 5). Although the importance of the carboxylate ion/
ligand in the palladation of both sp3 and sp2 C-H bonds
has been recognized,6 in this case both the cation and anion
play an essential role.7 For example, both potassium acetate
and cesium trifluoroacetate provided low amounts of the
product (Table 1, entries 4 and 6, respectively).8 However,
even with CsOAc the reaction efficiency was low, affording
48% yield of the desired product as well as 28% yield of
biphenyl. It became clear that biphenyl formation represented
a key competitiVe process responsible for consuming the
iodobenzene before full conVersion of the substrate could
occur.
The palladium-catalyzed Ullmann coupling is a well-
established protocol;9 moreover, it represents a frequently
encountered problem in hetero cross-coupling reactions such
as the Heck reaction and related processes.10 Surprisingly,
this issue has not been previously addressed in this context,
and thus there are no general guidelines available to mitigate
biphenyl byproduct formation. Consequently, we proposed
a qualitative kinetic model of the reaction system presented
here, which in turn guided our optimization studies (Figure
1).
Figure 2. Chemical yield and TON as a function of catalyst loading
in reaction of N-methylindole and Ph-I: Pd(OAc)2/PPh3 (1:4), 2.54
M in substrate, CsOAc, DMA, 125 °C, 24 h.
(starting from 5 mol % Pd) led to a steady increase of the
product yield at the expense of biphenyl formation, reaching
a maximum at 0.5 mol % Pd (Figure 2). The inverse
relationship between the catalyst loading and the chemical
yield is highly desirable, particularly at the lower range of
catalyst loading as observed herein.12
Lowering the catalyst amount below 0.5 mol % led to a
sharp decline in yield, which was accompanied by a dramatic
increase in the catalyst turnover number (Figure 2). At such
low concentrations, catalyst decomposition processes, includ-
ing biphenyl formation were suppressed. However, the
reaction rates were too slow to afford practical yields within
We surmised that the first step, namely, oxidative addition,
proceeds to an aryl-palladium halide intermediate, which may
(6) (a) Dangel, B. D.; Godula, K.; Youn, S. W.; Sezen, B.; Sames, D. J.
Am. Chem. Soc. 2002, 124, 11856-11857. (b) Sezen, B.; Franz, R.; Sames,
D. J. Am. Chem. Soc. 2002, 124, 13372-13373.
(7) Campo, M. A.; Larock, R. C. J. Am. Chem. Soc. 2002, 124, 14326-
14327.
(8) See Supporting Information for a broader exploration of the base
dependence.
(9) (a) Dyker, G.; Kellner, A. J. Organomet. Chem. 1998, 555, 141-
144. (b) Albanese, D.; Landini, D.; Penso, M.; Petricci, S. Synlett 1999,
199-200. (c) Hassan, J.; Penalva, V.; Lavenot, L.; Gozzi, C.; Lemaire, M.
Tetrahedron 1998, 54, 13793-13804.
(10) (a) Mitsudo, T.; Fischetti, W.; Heck, R. F. J. Org. Chem. 1984, 49,
1640-1646. (b) Andersson, C. M.; Larsson, J.; Hallberg, A. J. Org. Chem.
1990, 55, 5757-5761. (c) Dyker, G. J. Org. Chem. 1993, 58, 234-238.
(d) Padmanabhan, S.; Gavaskar, K. V.; Triggle, D. J. Synth. Commun 1996,
26, 3109-3113. (e) Shmidt, A. F.; Khalaika, A. Kinet. Catal. 1998, 39,
803-809. (f) Shmidt, A. F.; Smirnov, V. V.; Starikova, O. V.; Elaev, A.
V. Kinet. Catal. 2001, 42, 199-204.
(11) (a) Amatore, C.; Carre, E.; Jutand, A. Acta Chem. Scand. 1998, 52,
100-106. (b) Ozawa, F.; Hidaka, T.; Yamamoto, T.; Yamamoto, A. J.
Organomet. Chem. 1987, 330, 253-263.
(12) Penalva, V.; Lavenot, L.; Gozzi, C.; Lemaire, M. Appl. Catal., A.
Gen. 1999, 182, 399-405.
2898
Org. Lett., Vol. 6, No. 17, 2004