ACS Catalysis
Letter
a
Table 1. Optimization with 1-Hexanol
deuteration (% yield) α; β
entry
conditions
(max % yield)
1
2
3
1 mol % 2, 120 °C, 24 h
10 mol % 2, 120 °C, 24 h
0.2 mol % 1, 110 mol % NaOH,
120 °C, 24 h
0; 0 (96.5)
80; 0 (96.5)
b
94; 20 (94.1)
Figure 1. Ru-pincer complexes relevant to the current study.
4
5
6
7
8
0.2 mol % 1, 10 mol % NaOH,
120 °C, 24 h
1 mol % 1, 300 mol % NaOH,
120 °C, 24 h
no catalyst, 110 mol % NaOH,
120 °C, 24 h
0.2 mol % 1, 20 mol % NaOH,
120 °C, 24 h
as in entry 7 under air, 0.1 mol % 1
78; 0 (96.5)
nitrogen atmosphere. We find, however, that air can be used
with no detrimental effects.
b
94; 14 (94.1)
The crux of the discovery lies in the fact that unlike earlier
systems reporting metal-catalyzed H/D exchange, our system is
very practical. It can be used without large amounts of air-
sensitive or expensive metal catalyst and can be envisaged as
being adoptable for large scale synthesis of industrially relevant
substrates. Upon complete deuteration, most alcohols can be
easily separated from the reaction medium and the catalyst by
neutralizing the reaction mixture and extracting the relevant
alcohol in an organic solvent, such as diethyl ether. Smaller
alcohols that form azeotropes with water, such as ethanol, need
to be separated from water and dried using well established
industrial and household methods.
no deuteration
92; 10 (94.1)
b
90; 10 (94.1)
a
Yields obtained by NMR via integration of unreactive CH3 groups or
dioxane internal standard. In parentheses is the theoretical maximum/
equilibrium deuteration possible with 0.4 mL of D2O. Trace (∼1%)
of sodium hexanoate was also formed.
b
showed that it is possible to get significant deuteration at the β
position, albeit with a side reaction producing ∼1% sodium
hexanoate. In an open system, with evolution of hydrogen gas,
sodium hexanoate would be the major product as per our
recent report (Scheme 1).12 It is easy to separate out this
byproduct by performing a simple extraction in an organic
solvent, such as diethyl ether, of the alcohol substrate, with the
acid salt remaining in the aqueous layer. However, in most
cases when the base loading is less than 100 mol %, a very small
trace of acid salt is obtained, or it is not detected.
Significantly, similar conditions were utilized in our very
recently reported catalytic transformation of primary alcohols
to carboxylic acid salts, utilizing water as an oxygen source, with
concomitant evolution of hydrogen gas (Scheme 1).12 In the
Scheme 1. Catalytic Transformation of Alcohols to
Carboxylic Acids
For most applications, the presence of deuterium in the β
position is not deleterious, and thus, we decided to utilize the
optimal 1-hexanol conditions (Table 1; entry 7) for most of the
primary alcohols. These conditions led to the full deuteration of
ethanol in both the α and β positions, which is particularly
interesting if the desired product is ethanol-d6 (Table 2; entry
3). A number of functional groups proved to be tolerant to the
deuteration conditions. For example, the amine substrate
(Table 2; entry 7) showed no deuteration at the carbons
next to the amine moiety, as checked by deuterium NMR,
although the overall deuteration at the alcohol was limited to
only ∼35%, meaning that for the amine entry, the catalytic
efficiency was compromised.
Secondary alcohols proved much more active (Table 3). At
room temperature, some deuteration at the α position was
already in evidence after 3 h; however, most of the precatalyst
remains insoluble and, thus, unactivated at room temperature.
Heating to 50 °C overnight allowed for full catalyst activation
and subsequent full deuteration of both the α and β positions.
Thiols and very electron-poor alcohols, such as CF3CH2OH,
showed almost no activity in deuteration, probably because of a
stronger Ru−O or Ru−S bond that stabilizes an intermediate
species. In contrast, electron-rich alcohols, including electron-
rich benzyl alcohol and 1,3-bis(hydroxymethyl)benzene, gave
full deuteration after just 18 h of heating under the standard
primary alcohol conditions.
current work, the reaction is performed in a closed system,
preventing dihydrogen removal from the reaction vessel, and
often requires less than stoichiometric amounts of base and
lower catalyst loadings, especially for secondary alcohols.
In addition to low catalyst loadings and relative simplicity of
use, our system is tolerant of a number of functional groups
that do not react with aqueous warm base, including amines,
unactivated double bonds and CF bonds.13 Impurities are also
well tolerated, as all substrates tested were used “as is” from the
manufacturer’s bottle without further purification. In a typical
reaction, 0.2% of the catalyst and 20% NaOH was put into a 2.5
mL NMR Young tube, to which the substrate and 0.4 mL of
D2O were added (note: higher loadings of D2O lead to higher
deuteration percentages). The reaction conditions were
optimized for the substrate 1-hexanol, for which the optimal
conditions led to full (highest percentage possible) deuteration
at the α carbon and small amounts of side deuteration at the β
position (Table 1). Temperature and amount of base play a
significant role in the selectivity, with the optimal conditions
differing depending on the substrate. For 1-hexanol, 10%
NaOH loadings gave the best selectivity, but reactivity was
slightly compromised. Really high base loadings (≥110%)
Base is essential for the reaction to proceed under low
catalyst loading, although it was found that the activated
complex 3, prepared by the reaction of dearomatized 2 with
D2O,14 could catalyze the deuteration of 1-hexanol at 10 mol %
449
dx.doi.org/10.1021/cs400092p | ACS Catal. 2013, 3, 448−452