12
M. Bagherzadeh et al. / Inorganic Chemistry Communications 44 (2014) 10–14
that the formation of the cross-coupled products initially increased
along with the progress of the reaction time, reached a maximum
after 9 h and then remained intact (Fig. 4S).
Since, high catalyst loading inhibits the catalytic reaction and low
palladium catalyst loading is required in some cases [17], using small
amounts of catalyst in order to achieve high conversions in the Heck
cross-coupling reactions is preferred. To ascertain the efficiency of the
catalyst, different catalyst to substrate ratios were tested in the coupling
reaction of styrene with iodobenzene in the presence of Pd/MnBDC as
catalyst and the results were summarized in Table 2. It was found that
a decrease in the amount of catalyst does not affect the yields of the re-
action and the use of 0.12 mol% Pd of catalyst still gives high conversion
and simultaneously, increased the Turnover number (TON). Achieving
high TON is one of the merits of this Pd supported catalyst.
The Heck coupling reaction of iodobenzene with various olefinic
substrates including either aromatic or aliphatic terminal alkenes with
electron-donating or electron-withdrawing substitution was also inves-
tigated using Pd/MnBDC catalyst (Table 3, entries 1–11). It was
observed that supported Pd-NPs on MnBDC function as an active cata-
lyst for the coupling reaction of iodobenzene with terminal alkenes
and show the desired E-isomeric products as the major product with
good to excellent yields. Comparing with styrene, 4-methylstyrene
and 4-methoxystyrene, electron-rich substituted, exhibited the lowest
activity in the process of coupling with iodobenzene (entries 1–3).
The α-methylstyrene gave a much lower conversion than unsubstituted
ones which is probably due to steric effect (entry 4). It is note worthy
that increase in hydrocarbon chain length of aliphatic alkenes has
no significant influence on yield of coupling products (entries 6–8).
In the case of methyl-2-hydroxyacrylate, electron-withdrawing
β-substituted processed lower coupling than electron-rich ones, ethyl
methacrylate (entries 9, 10).
The mechanism for the reaction of iodobenzene with terminal
alkynes catalyzed by Pd/MnBDC is proposed on the basis of the mecha-
nism of previous reports [18] and our results, as shown in Scheme 1. The
catalytic cycle begins with the oxidative addition of iodobenzene to
supported Pd-NPs to form σ-arylpalladium intermediate A. The syn-
migratory insertion of alkyne to A leads to the formation of B intermedi-
ate followed by an internal rotation case which creates C intermediate.
The comparison between the results of α-methylstyrene and styrene
coupling reactions with iodobenzene (Table 3, entries 1, 4) further con-
firms the B intermediate formation. The large energy barrier to internal
rotation favors the production of E-isomeric products (note to % selec-
tivity in Table 3). The hydridopalladium halide D is formed by syn-β
hydride elimination of C or B. In the last step, the catalytic cycle is
completed by reductive elimination of H–Pd–I intermediate (D) in the
Fig. 4. TEM images of supported Pd-NPs on MnBDC.
3
a conclusion, Et N as base in DMA solvent at 90 °C is the optimized con-
dition for the coupling reaction in current catalytic system. Although
aryl iodides react readily, aryl bromides and chlorides are considerably
less reactive (conversion of 60% and 35% respectively) due to the
stronger carbon–halogen bond.
The formation of trans-stilbene from the cross-coupling reaction of
styrene with iodobenzene as a function of time displayed indicates
Table 1
Optimization of the reaction conditions in cross coupling reaction of iodobenzene and
a
styrene in the presence of Pd/MnBDC.
% conversionb
% selectivityc
presence of Et
3
N as base to remove HI from the D and palladium (0) is
Entry
Solvent
Base
reformed. The ultimate outcome of this catalytic cycle is C\C coupled
products.
1
2
3
4
5
6
7
8
9
DMSO
DMF
DMA
Et
Et
Et
Et
Et
3
N
N
N
N
N
CO
CO
CO
85
92
97
89
90
92
85
70
88
88
85
85
90
91
87
89
88
–
3
We conducted the control experiments to confirm that the reaction
was indeed catalyzed by Pd/MnBDC instead of free Pd-NPs, since some
of active sites in solid catalyst could dissolve into the solution during
the course of the reaction. In several cases, these leached species from
the solid catalyst could contribute dramatically to the total conversion
of the reaction [19]. So, the catalytic coupling reaction iodobenzene
with styrene was carried out in DMA for 9 h at 90 °C using 0.16 mol%
catalyst. After the reaction, the catalyst was simply separated from the
reaction mixture by centrifugation. The reaction solution was trans-
ferred to a new vessel, and fresh reagents were then added to the
solution. The resulting mixture was stirred at 90 °C. Only less than 8%
conversion was observed after 24 h. These results confirmed that the
coupling reaction could only proceed in the presence of the solid cata-
lyst, and there was no contribution from leached active species in the
liquid phase.
3
d
3
CH CN
3
65
p-Xylene
DMSO
DMF
DMA
DMSO
DMF
DMA
DMA
DMA
DMA
DMA
DMA
3
21
70
78
80
76
90
92
15
13
K
K
K
2
3
2
2
3
3
NaCH
NaCH
NaCH
Pyridine
Pyrrolidine
3
3
3
CO
CO
CO
2
10
11
12
13
14
15
16
2
2
e
Et
Et
3
N
N
70
f
3
1
–
1
–
a
Reaction condition: 13 mg Pd/MnBDC (0.12 mol% Pd), styrene 1.1 mmol,
iodobenzene 1 mmol, base 1.5 mmol, temperature 90 °C, after 9 h.
b
Determined by GC, based on iodobenzene; average of two runs.
Selectivity to trans-stilbene.
Solvent boiling point.
Temperature 70 °C.
c
d
The recycling of the catalyst is one of the significant aspects for prac-
tical applications. Therefore, the recyclability of the Pd-NPs supported
catalyst was investigated in reaction of styrene with iodobenzene in
e
f
Reaction without catalyst.