Table 1. Different temperature addition
int. 2 int. 3 yield purity A%
entry (equiv) (°C) (equiv)
offer at least two main advantages. First, being the top phase
in the separation process allows quicker extraction (obviating
the need for a second reactor) and also allows the reactor to be
kept relatively dry. Second, DCM requires a very efficient
condensation plant for recovery. Usually, the recovery ratio does
not exceed 35-40% for DCM, while EtOAc could be recycled
almost entirely. We focused on the homogeneous phase reaction
because of the quicker reaction time. Following the positive
results obtained, we decided to apply this synthetic procedure.
The HEL parallel synthesis apparatus also allowed us to
obtain preliminary calorimetric data. Although the studies were
not expressly designed for this purpose (and thus must be
considered as indicative), a small exothermic effect was
nonetheless observed when DIPEA was added, increasing with
addition of thiophenol. The molar heat was estimated at 159.27
kJ or 38.10 kcal (based on dose of 1.76 g of 3,5-difluo-
rothiophenol).
We moved to the following step for the oxidation of sulfide
to sulfone, see Scheme 3. The intermediate 4 does not need to
be isolated, and it can be used directly as solution in the
oxidation process, with savings in time and resources. According
to the original synthetic procedure, it was made by using HIO4
(cat. Cr2O3). For obvious environmental issues and scale-up
considerations, this oxidation reactant was abandoned. After
having considered other reagents5 (e.g., urea/H2O2,6 H2O27), we
focused on investigating the use of Oxone8 (potassium monop-
ersulfate triple salt technical grade; KHSO5 47%) as oxidizing
agent. Oxone has the main advantage of being an inexpensive
reagent easily removed by workup, while it suffers from the
drawback of the relatively high amount of product that it is
necessary to use in relation to the oxygen content.
Different conditions of solvent, temperature, time, and molar
ratio were investigated for Oxone; the results are reported in
Table 3. Entry 1 shows that in N,N-dimethylformamide (DMF)
the reaction is relatively fast, being virtually completed after
6 h. Moving to a mixture of water/ethyl acetate, entry 2, the
sulfide is transformed relatively rapidly into the sulfoxide 4a,
but oxidation to sulfone 5 does not go to completion, as the
reaction runs in heterogeneous phase. The addition of a phase
transfer catalyst (i.e., Bu4NBr) and an extra amount of fresh
Oxone does not significantly improve the conversion. We
needed to improve the workup because, when water is added,
the product tends to crash out in lumps, trapping unreacted
Oxone salts, see entry 3. Dissolution in organic solvent was
T
14
by HPLC (A%)
%
1
2
3
4
5
1.0
1.0
1.0
1.0
1.0
-40
-3
0
1.00
1.15
1.15
1.15
1.15
95.5
98.9
100.0
94.3
90.3
98.6
98.1
98.4
98.1
98.0
0.24
1.03
0.90
1.20
1.14
0
25
solvents, bases, and molar ratios were evaluated by experiments
using the HEL parallel synthesis instrument, which allowed us
to run four reactions simultaneously.
A set of reactions were made that compared the original
procedure at different temperatures, the results of which are
reported in the Table 1. We noted that the reaction reaches
complete conversion within 2 h and 30 min, with no need to
react overnight. Entries 2-5 show that the addition between
-3 and 25 °C does not seem to significantly alter the content
of 14, the formation of which is actually more linked to the
equivalent (equiv) of thiophenol used within the reaction. In
entry 1, where we used 1.0 equiv it was significantly lower;
Cs2CO3 was used in the ratio of 1.1 equiv for all experiments.
Additional tests were performed for base and solvent
screening as reported in Table 2.
In entry 1 the reaction used for byproduct 14 isolation is
reported. The use of DCM gave promising results in terms of
yield and purity, achieving lower byproduct formation (see entry
3 versus entry 2). The calculated pKa for 3,5-difluorothiophenol
is 5.09 ( 0.11, which means that a strong base was not needed.
Upon general consideration usually 4 log units between the acid
and the base are sufficient to obtain a complete dissociation of
the species. Literature4 values show: pKa t-BuOK (19), EtONa/
MeONa (18), Na2CO3 (10), R3N (10). It is possible to reduce
the amount of cesium carbonate, and this represents a significant
economic advantage; see entries 4 and 5. We considered the
use of more economic carbonate and the switch to a homoge-
neous reaction in order to achieve a more efficient conversion.
As shown in entry 6 the homogeneous reaction obtained using
N,N-diisopropylethylamine (DIPEA) is faster and gives good
yield and quality product. The use of cheaper carbonates does
not appear to give a real advantage and notably results in a
worse impurity profile, possibly due to the higher reaction time,
see entries 7 and 8. These carbonates left a certain degree of
unreacted starting material, whereas cesium carbonate worked
quite well. This might be explained by the low polarity of DCM
versus that of the THF used previously, and possibly by the
potential impact of the particle size of the bases: Cs2CO3 is a
very soft powder with very small grain/crystals, while other
carbonates have larger particle size. In entry 9 we tested sodium
carbonate (Na2CO3) with an ethyl acetate (EtOAc)/water solvent
mixture in the attempt to speed up the reaction because of better
dissolution of the carbonate (bearing in mind, however, that
these two solvents are not completely miscible at alkaline pH).
The reaction is in fact faster, but unreacted starting material is
increased. This may be due to a moderate degradation of 3,5-
difluorothiophenol in water (e.g., oxidation effects) limiting
reaction completion. In entry 10 we further investigated the use
of ethyl acetate as solvent. On a plant scale this solvent would
(5) Caron, S.; Dugger, R. W.; Ruggeri, S. G.; Ragan, J. A.; Brown Ripin,
D. H. Chem. ReV. 2006, 106, 2943–2989.
(6) Cooper, M.; Heaney, H.; Newbold, A. J.; Sanderson, W. R. Synlett
1990, 533–535.
(7) (a) Shokrolahi, A.; Zali, A.; Pouretedal, H. R.; Mahdavi, M. Catal.
Commun. 2008, 9 (5), 859–863. (b) Bahrami, K. In Regio- and stereo-
controlled oxidations and reductions; Roberts, S. M., Whitall, J., Eds.;
Catalysts for Fine Chemical Synthesis, Vol. 5; Wiley: Chichester,
England; Hoboken, NJ, 2007; pp 283-287. (c) Shaabani, A.; Rezayan,
A. H. Catal. Commun. 2007, 8 (7), 1112–1116. (d) Velusamy, S.;
Kumar, A.; Saini, R.; Punniyamurthy, T. Tetrahedron Lett. 2005, 46
(22), 3819–3822.
(8) (a) Ward, R. S.; Roberts, D. W.; Diaper, R. L.; Richard, L. Sulfur
Lett. 2000, 23 (3), 139–144. (b) Kropp, P. J.; Breton, G. W.; Fields,
J. D.; Tung, J. C.; Loomis, B. R. J. Am. Chem. Soc. 2000, 122 (18),
4280–4285. (c) Llauger, L.; He, H.; Chiosis, G. Tetrahedron Lett. 2004,
45 (52), 9549–9552.
(4) Comer, J. Chem. Br. 1994, 983–986.
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Vol. 13, No. 3, 2009 / Organic Process Research & Development