Journal of the American Chemical Society
Article
phase boundary (i.e., the non-enantioselective on-water
catalytic effect) can negatively influence enantioselectivity.10e,16
Therefore, to achieve successful enantioselective catalysis in
water, it is important to suppress the hydrogen bonding
interactions of water molecules at the enantio-determining
step. The use of a hydrophobic cosolvent represents one of the
simplest means of achieving this end; the hydrophobic
cosolvent shields the transition state from contact with water.14
To our delight, the addition of CPME as a hydrophobic
cosolvent additive yielded markedly enhanced enantioselectiv-
ity. For example, using catalyst 5a, the enantioselectivity was
increased from 38% ee to 74% ee by adding 5 equiv of CPME
(Scheme 1B). With these encouraging results, a number of
hydrophobic cosolvents were further screened using 5a as
catalyst, and it was found that eucalyptol, a natural cyclic ether
and a monoterpenoid, proved optimal with respect to both
chemical yield and enantioselectivity of the desired product
(Scheme 1C and Supporting Information, Table S1). Using
eucalyptol as a hydrophobic cosolvent, we then evaluated the
effect of thiol structures on reaction rate and enantioselectivity.
Regardless of the degree of substitution, alkyl thiols were found
to serve as general GSH surrogates in terms of enantiose-
lectivity (Scheme 1C and Supporting Information, Figure S1).
Notably, the enantioselectivity of alkyl thiols increases with the
steric bulkiness of the substituent. Thus, a significant
enhancement in enantioselectivity was observed when the
substituent was changed from a primary to a tertiary alkyl
group (from 77% to 87% ee). However, when tertiary butyl
thiol was used, the reaction rate decreased dramatically due to
the steric effect (only 18% conversion after 24 h) (Scheme
1C). The problem of low conversion was easily addressed by
increasing the molar ratio of thiols. With 10 equiv of thiols, the
reaction could be completed after 4 days and, moreover,
increased ee values were obtained (for example, an ee of 4ad
from 87% to 91%) (Supporting Information, Table S2).
Condition Optimization Using Biphasic Microfluidic
Conditions. As described, the use of a hydrophobic cosolvent
was pivotal in achieving high enantioselectivity; this is ascribed
to the “spatial separation” of water from the transition state.
Nevertheless, under stirred conditions, it is difficult to perfectly
suppress the negative interfacial hydrogen bonding interaction
between the aqueous phase and organic reactants, since new
organic-water interfaces are constantly regenerated as a result
of stirring. We hypothesized that this problem could be
addressed by employing a biphasic microfluidic system, where
precisely defined micron-sized monodisperse water and
organic plugs could easily be generated in a tube reactor.15,17
Under static conditions in a tube reactor, new organic-water
interfaces cannot be recreated during the reaction and, thus,
the interfacial surface area must be incomparably smaller than
the interfacial surface area generated with stirring, con-
sequently minimizing the contact area between bulk water
molecules and the transition state. Furthermore, the diffusion
process of protons in water might be influenced by the
confinement effect.18 According to recent studies using
polarization-resolved femtosecond infrared transient absorp-
tion spectroscopy, in nanosized confined water droplets, the
diffusion rate of protons is significantly slower than that in bulk
water.18 Considering all these assumptions, catalytic isomer-
ization of the hemithioacetal 3aa, spontaneously generated
from 1a and 2a, was performed as a model reaction in a
biphasic microfluidic system (eucalyptol/brine).
This system was set using a cross-junction meeting of
controlled flows of brine and organic solutions containing the
organic reactants (1a and 2a) and catalyst 5a. The reaction
mixture was injected into the system using a syringe pump. A
series of droplets of different sizes were created in the
hydrophobic tubing (fluorinated ethylene propylene, FEP,
inner diameter (ø) = 500 μm, length = 15 m) by adjusting the
flow rate ratio (Qw/Qo) between the aqueous and organic
phases (Scheme 2A). After the tube was filled with the reaction
a
Scheme 2. Microfluidic Experiments
a
(A) Biphasic microfluidic system for isomerization of hemithioacetal
3a. Conditions: phenyl glyoxal 1a (0.1 mmol), benzyl thiol 2a (1
mmol), catalyst 5a (30 mol %), and eucalyptol (10 equiv): plugs form
at the junction between eucalyptol solution containing the reagents
(organic phase) and an aqueous phase (brine). Plugs then travel down
the FEP tubing where the reaction occurs. (B) Reaction profiles under
different conditions. (C) Effect of biphasic microfluidic conditions on
enantioselectivity. Conditions: (a) magnetic stirring (1150 rpm),
brine (2 mL), eucalyptol (10 equiv), 20 °C. (b) Microfluidic
condition (Qo:Qw = 6:120 μL/min) in ø = 500 μm FEP tubing, 20 °C.
(c) microfluidic condition (Qo:Qw = 6:120 μL/min) in ø = 500 μm
FEP tubing, 20 °C, 150 psi BPR. *The isolated yields could not be
determined since the total amount of organic reaction mixture in the
micro-tube was too small to determine the correct yield. Thus, we
determined the conversions using 1H NMR integration instead of
isolation yields.
mixture, the flows of brine and organic solutions were stopped,
and the outlet of the tube was then sealed with paraffin film.
The static biphasic plugs were then kept inside the tubing for
96 h at 20 °C, without any shaking. Gratifyingly, the reactions
proceeded smoothly even in the static droplets. The reaction
profile in the static droplets is almost the same as that observed
under the conventional stirring condition (Scheme 2B) (see
Supporting Information, Table S3, for additional experimental
2554
J. Am. Chem. Soc. 2021, 143, 2552−2557