Organic Letters
Letter
Scheme 2. Electrochemical Reaction Mechanism for the
Synthesis of Azoxy and Azo Compounds
azoxy compound. It should be noted that, in addition to 3, the
oxidation of water at the anode causes the balance of electrons.
The reaction mechanism for the synthesis of azo compounds
(6) is similar to that of azoxy compounds, except that the
azoxy compound in the next step is reduced at the cathode and
converted to the azo compound by removing a water molecule
(Scheme 2). According to the Scheme 2, two molecules of
ortho-halonitrobenzene and 10 electrons are needed to
synthesize each molecule of the azo compound. Therefore,
in this case, theoretically 5 electrons are consumed per ortho-
halonitrobenzene molecule. However, in the experiments we
performed in an undivided cell, due to the occurrence of
phenomena such as the back reaction, the number of electrons
was 6 for each ortho-halonitrobenzene molecule. The reduction
of the ortho-azoxy compounds may be related to the higher
solubility of these compounds compared to para-azoxy
compounds (SI, pages S16 and S18). In addition, the observed
cathodic peak C−1 in Figure 2, part III, is due to the reduction
of the ortho-azoxy compound to the ortho-azo compound.
In order to prove the proposed mechanism, the synthesis of
azoxy (or azo) compounds was also examined under exactly
the same conditions in a divided cell (Figure 3). The results
clearly show that no trace of the formation of the azoxy (or
azo) compound was observed when a divided cell is used. In
other words, the participation of the anodic process in product
formation is essential.
To improve the synthetic efficiency, the synthesis of azoxy
and azo compounds was also studied under constant current
conditions. The effect of current density on the yield of 5a was
initially investigated (SI, page S14). These experiments were
performed under the following conditions: charge consumed,
4.0 F; 1a amount, 1.0 mmol; solvent, water (0.2 M phosphate
buffer, pH = 3.0)/acetonitrile (50/50 v/v) mixture. The results
show that the optimum value for the current density is 1.2
mA/cm2 (Iapp = 40 mA). In this current density, the yield of
79% was obtained for the synthesis of 5a. Insufficient applied
potentials for the formation of N-(4-bromophenyl) hydroxyl-
amine at low current densities can be the reason for the low
yield under these conditions. On the other hand, the over-
reduction of 1a at the cathode, overoxidation of N-(4-
bromophenyl)hydroxylamine at the anode, and reduction
and/or oxidation of 5a (or solvent) are the main factors in
decreasing the product yield at higher current densities.
The effect of charge consumed on the yield of 5a was also
investigated (SI, page S14). These experiments were
performed under an optimum current density of 1.2 mA/
Figure 3. Constant current electrolysis of 2a (0.5 mmol) in undivided
(above) and divided (below) cells in acetonitrile/water (containing
0.2 M phosphate buffer, pH = 3.0) mixture (50/50 v/v), at room
temperature. Japp = 1.2 mA/cm2 (Iapp = 40 mA).
cm2. The results show that the optimum value for the charge
consumed is 4.0 F which is the theoretical amount of electricity
necessary for the reduction of 1.0 mmol of 1a (Scheme 2). It
seems that the reduction and/or oxidation of 5a are the main
factors in decreasing the product yield at higher charge
consumed. The effect of solution pH (in the range 2−6) on
the yield of 5a under optimum conditions was also studied.
Our results show that the highest yield and purity of products
were obtained at pH 3.0. Similar optimizations were also
performed for the synthesis of 6a. These experiments were
performed on 2a and yielded similar results to those obtained
for 5a. The only significant difference was in the amount of
electricity consumed. In this case, the optimal amount of
electricity needed for the synthesis of 6a was 6.0 F (slightly
more than the theoretical value of 5.0 F). Under these
conditions, the yield of 64% was obtained for the synthesis of
The effect of anode and cathode materials was also studied
on the yield of 5a. The results of this series of experiments are
shown in Table 1. As can be seen, the maximum yield of 79%
was obtained, when carbon is used for both the anode and
cathode.
Table 1. Dependence of 5a Yield on Electrode Material
entry
cathode
Carbon
Carbon
Carbon
Stainless Steel
Zn
Fe
Cu
anode
Carbon
Stainless Steel
Cu
Carbon
Carbon
Carbon
Carbon
yield [%]
79
31
1
2
3
4
5
6
7
no reaction
62
38
57
50
C
Org. Lett. XXXX, XXX, XXX−XXX