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Table 1: Results of the electrochemical bromination of cyclohexene in
a linear paired electrolysis.
the oxidation of furane in up to 195% current efficiency were
never published elsewhere and represent the basis for this
investigation (Scheme 3).
As a catalyst for the reduction of molecular oxygen a N-
methylated 1,10-phenanthroline-5,6-dione catalyst (3;
PDMe) was utilised and in methanol solution furane was
converted to the dimethoxy derivative 4 in good overall yield.
However, when we adopted this reaction for the bromination
of cyclohexene[6,7] we recognised some inconsistencies. The
outline of the desired reaction is shown in Scheme 4.
Entry
Variations from initial conditions
Yield[a]
1
2
3
4
5
6
7
8
none
75% (ce: 150%)
79% (ce: 158%)
66% (ce: 131%)
80% (ce: 160%)
81% (ce: 162%)
24% (ce: 48%)
35% (ce: 70%)
71% (ce: 142%)
81% (ce: 162%)
65% (ce: 130%)
67% (ce: 134%)
81% (ce: 162%)
95%[d] (ce: 190%)
À58C
158C
electrode distance: 9 mm[b]
glassy carbon cathode (1.50 cm2)[c]
Pt anode (1.50 cm2)
both electrodes (1.50 cm2)
7.5 mA
9
12 mA
0.1 m H2SO4
0.3 m H2SO4
150 rotations/min
250 rotations/min
10
11
12
13
Scheme 4. Quinone-mediated linear paired electrolysis for the bromi-
nation of cyclohexene.
Unless otherwise stated, the reactions were performed in an undivided
cell with a platinum anode (active surface area: 2.55 cm2) and a glassy
carbon electrode (active surface area: 2.55 cm2) with an electrode
distance of 11 mm on a 0.5 mmol scale. The reaction mixture was
saturated with oxygen for 10 minutes at 08C prior to electrolysis. [a] The
yield was determined by GC analysis of the crude reaction mixture using
mesitylene as internal standard. [b] This change was kept for entries 5–
13. [c] This change was kept for entries 6–13. [d] Isolated yield.
The current demand for high efficiencies in chemistry and
the preservation of energy in general are of high interest.
Therefore, the perspective of doubling the efficiency of
a chemical reaction by an innovative technique, such as
a linear paired electrolysis, was investigated.
A linear paired electrolysis is principally performed in an
undivided cell design and passing 1.0 F through the solution
would result in complete conversion of the cyclohexene giving
a 200% current efficiency. However, when the reaction is
performed in a divided cell, the efficiency of the anodic as
well as the cathodic reaction can be determined independ-
ently. Also, in a divided cell 2.0 F have to be passed through
the solution to obtain theoretical 100% conversion. Accord-
ingly, the optimisation of the linear paired electrolysis was
first conducted in a divided cell and later in an undivided cell
to determine the efficiency of the coupled processes. In fact,
the presence of quinones, such as 3 or anthraquinone, which
was reported to facilitate the formation of H2O2,[8] proved to
be effective for the bromination of cyclohexene in the cathode
compartment but the effect was marginal, so that the further
reactions were conducted in the absence of these quinones
(for details, see SI).
(À12 to + 208C). Afterwards, the influence of the electrode
distance (1–3 cm), the electrode surface (3.5–6.0 cm2), the
current (5–15 mA), and the stirring rate (150–750 rpm) were
examined. The best results for the temperature dependence of
the reaction were obtained at À58C, but for general
convenience, we decided to perform the electrolysis at 08C
with an ice bath and not at higher or lower temperatures
(Table 1, entries 1–3). The product generation was mostly
influenced by the surface areas of the electrodes (Table 1,
entries 4–7), less by the electrode distance or the electrode
material itself. Reducing the electrode surface of the platinum
anode by about 50% resulted in almost doubling of the
current density and led to low overall performance while
small variations of the current (Table 1, entries 8/9) had
a comparable little effect. With respect to yield and current
efficiency the amount of sulfuric acid was found to be optimal
at 0.2 m. A factor that is quite relevant and is overlooked (or
irrelevant) in many organic reactions is the stirring rate (the
size of the stir bar[10] was kept constant), which intensively
affects the mass transport. An electrochemical short-cut
(oxidising bromide to bromine at the anode, transport to
the cathode and reduction of bromine to bromide—or the
oxidation of H2O2 at the anode) had to be avoided. Therefore,
we checked the stirring rate as well and the best results were
obtained when 250 rpm were applied. Slower stirring might
cause a too slow mass transport of the cathodically generated
H2O2 into the bulk solution where Br2 is formed. If this
process happens near the cathode, reduction of Br2 to
bromide can occur and a reduced current efficiency is
The oxidation of bromide to bromine in the anode
compartment of a divided cell, where bromine equilibrates
with the tribromide anion (Br3 ),[9] proved to be uncritical and
À
therefore, we turned our attention to the cathode compart-
ment to optimise the reduction of oxygen to H2O2 to produce
bromine as well. The preliminary optimisation of the cathodic
oxidation reaction was performed in a divided cell under
oxygen atmosphere to verify good starting conditions for this
part of the electrolysis. Subsequently, the extensive optimisa-
tion was realised in an undivided cell design and is summar-
ised in Table 1 (for further results see SI). First, we tested
several bromide sources (NaBr, KBr, and nBu4NBr) and
solvents (DMF, TFE, HFIP, and CH3CN) and their water
content (0–20 equiv), as well as the reaction temperature
Angew. Chem. Int. Ed. 2021, 60, 9996 –10000 ꢀ 2021 The Authors. Angewandte Chemie International Edition published by Wiley-VCH GmbH www.angewandte.org 9997