Organic Letters
Letter
high solubility in aqueous acid. In CV studies of 1, the different
redox couples are more clearly distinguished in aqueous
perchloric acid than in aqueous triflic acid; thus, the reaction
was optimized using the former.10,12 Several parameters were
altered in an effort to find optimal electrochemical reaction
conditions, including the choice of electrode materials, cell
configuration, and electrochemical settings (i.e., controlled
potential vs constant current electrolysis).
Electrochemical oxidation of 2-amino-6-methylheptane by 1
does not proceed in an undivided cell. The inability to effect
hydroxylation of this substrate presumably arises from
unproductive reduction at the cathode of the Ru species, all
of which are more readily reduced than protons based on their
differing redox potentials.13 Thus, a H-cell with the anodic and
cathodic chambers separated by a fine glass frit was employed
for all subsequent screening. In this divided cell, the reaction
contents are loaded into the anodic chamber with 4 mL of 1:1
AcOH/0.75 M aqueous HClO4; an equivalent volume of 1:1
AcOH/0.75 M aqueous HClO4 is added to the cathodic
chamber.
Electrochemical oxidation was initially attempted by
controlled potential bulk electrolysis to generate a discrete
RuV-based oxidant. Our previous mechanistic studies showed
that one pathway for catalyst arrest involved ligand dissociation,
a reaction postulated to ensue from a RuVI dioxo species.9,10
Notably, oxo species of both RuVI and RuV were established as
active catalysts, but ligand dissociation is only believed to occur
from the former.9 Accordingly, we envisioned employing
controlled potential electrolysis to selectively generate a RuV
oxidant in order to suppress the putative catalyst decomposition
pathway. In practice, however, controlled potential electrolysis
required excessively long reaction times as a consequence of
sluggish electron transfer kinetics at the anode (Table 1, entries
3 and 4). This result is not particularly surprising given that
relatively slow CV scan rates (<50 mV/s) are necessary to
observe clear redox events with 1.
Figure 2. Cyclic voltammogram (CV) of 1 mM cis-[(dtbpy)2Ru-
(CO3)]11 in 1:1 AcOH/0.75 M aqueous HClO4 at a 10 mV/s scan rate
using a glassy carbon working electrode, platinum mesh counter
electrode, and SCE reference electrode.
can be readily accessed through outer-sphere oxidation, thus
motivating the development of an electrochemical protocol for
C−H hydroxylation. The operation of 1 in aqueous acid was
also considered advantageous for the development of an
electrochemical method, as the ionic medium would serve as
supporting electrolyte. Accordingly, no screening of supporting
electrolyte was necessary. Furthermore, the strongly acidic (pH
< 1) aqueous conditions enabled simple proton reduction (2H+
+ 2e− → H2) to function as the cathodic reaction (Figure 1), a
notable difference between electrocatalysis in aqueous versus
nonaqueous solvents. The latter requires addition of a
supporting electrolyte salt, and the precise reaction occurring
at the counter electrode is often unclear.
Initial proof-of-concept studies focused on establishing the
feasibility of the electrochemical hydroxylation by 1 with a
commercially available model substrate, 2-amino-6-methylhep-
tane (Table 1). This primary amine substrate was selected for its
Table 1. Analysis of Electrolysis Conditions for C−H
a
Hydroxylation
A marked improvement in reaction performance was noted
by switching from constant potential to constant current (CC)
bulk electrolysis. Performing the CC electrolysis reaction with
2-amino-6-methylheptane at 10 mA for 6 h afforded a > 2-fold
increase in product yield (Table 1, entry 6). Further
optimization of this process focused on examining a range of
fixed current values for electrolysis. Ultimately, it was
determined that performing the reaction at 25 mA for 6 h
afforded product in a yield comparable to the optimized
chemical oxidation with H5IO6 (Table 1, entry 1 vs 2).
Controlling the current, rather than performing electrolysis at
constant potential, forces the reaction to proceed by applying a
larger overpotential.14,15 Monitoring the potential through
inclusion of a SCE reference electrode in the anode compart-
ment reveals that the applied potential is 2.5 V when the
reaction is performed at 25 mA. This potential is substantially
higher than the redox potentials measured by CV for generating
the high valent Ru statesthe applied potential is over 1 V
higher than the onset potential for generation of RuVI. The need
for such a large overpotential reflects the slow electron transfer
kinetics for outer-sphere oxidation of the Ru catalyst.16
b
entry
deviation from standard conditions
none
chemical oxidant conditions
1.34 V vs SCE (RuVI), 24 h
1.27 V vs SCE (RuV), 24 h
4 h
10 mA
10 mA, 14 h
20 mA, 14 h
35 mA
yield (%)
1
2
3
4
5
6
7
8
63
65
15
<5
36
35
51
63
51
30
0
c
9
10
11
12
13
14
50 mA
no cis-Ru(dtbpy)2Cl2
2.5 mol % cis-Ru(dtbpy)2Cl2
no current
48
0
<5
undivided cell
Having identified optimal conditions for controlled current
electrolysis, we next examined the scope of this electrochemical
C−H hydroxylation protocol. A variety of structurally disparate
substrates tested in our earlier report were assessed under the
electrochemical protocol for direct comparison of the efficiency
of inner- versus outer-sphere oxidation.4 Overall, the electro-
a
b
Reactions conducted on a 0.24 mmol scale. Percent yield
1
determined by H NMR integration of unpurified reaction mixtures
versus 4-nitrotoluene as internal standard. Chemical oxidant
conditions: 5 mol % of cis-Ru(dtbpy)2Cl2, 2 equiv of H5IO6, 1:1
AcOH/H2O, 6 equiv of TfOH, 4 h. SCE = saturated calomel
electrode.
c
B
Org. Lett. XXXX, XXX, XXX−XXX