Angewandte
Research Articles
Chemie
the need for prolonged bubbling into a solvent for saturation;
2) the choice of reaction solvent is limited by the gas
Table 1: Selected entries for optimization studies toward continuous
flow gem-difluoroalkenylation.
[
a]
(
solubility; (3) the release of gas into the system headspace
during the reaction; (4) the lengthened reaction time caused
by insufficient gas-liquid interfacial contact or continuous
bubbling into the mixture, and (5) safety concerns and
scalability issues. With our continuing interest in flow
[
16]
methodology development, we were intrigued to address
these limitations by using mircoflow technology. Flow proc-
essing provides many advantages relative to batch tech-
Entry
LiOt-Bu
[equiv]
ClCF H
[equiv]
T
[8C]
Solvent
tR
[min]
Yield
[%]
2
[16,17]
[
b]
niques
including the enhanced reactivity through im-
proved heat and mass transfer, steady-state small scale
generation with immediate consumption of unstable/hazard-
ous reagents, and facile pressurization for significantly
increased gas-liquid interfacial contact.
Herein, we report a modular continuous flow platform for
both deuteriodifluoromethylation and gem-difluoroalkenyla-
1
2
3
4
5
6
7
8
9
2.0
2.0
2.0
2.0
2.0
2.0
2.0
1.5
1.5
2.0
2.0
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.0
3.0
3.0
60
40
20
0
0
0
0
0
0
0
THF
THF
THF
THF
THF
2-MeTHF
CPME
2-MeTHF
2-MeTHF
2-MeTHF
2-MeTHF
15.0
15.0
15.0
15.0
7.5
7.5
7.5
7.7
7.7
47
57
70
80
74
76
61
74
68
79
82
tion of aldehydes using the ClCF H gas (Figure 1d). Different
2
downstream processing modules in the flow system diverts the
fate of the difluorinated oxaphosphetane (OPA) intermediate
to give desired products. The method is rapid, scalable and
exhibits a broad substrate scope.
1
11
0
7.5
12.0
0
[
[
a] Please see Supporting Information for detailed optimization tables.
b] GC-FID yields were reported.
Results and Discussion
literature precedents on the Wittig gem-difluoroalkenylation
[22c–e]
employed high reaction temperatures,
we postulated that
We initiated our study by investigating the use of ClCF H
the enhanced heat transfer might also accelerate the disso-
ciation of the ylide as well as dimerization of difluorocarbene
2
gas for the gem-difluoroalkenylation of aldehydes in flow.
gem-Difluoroalkenes are valuable synthetic intermediates
towards functional organic materials and pharmaceutically
[
23]
to form tetrafluoroethylene. We found that a decrease in
temperature improved the reaction yields with 08C being the
optimal (Table 1, entry 1–5). This is presumably due to the
stabilization of the transient ylide. The use of subzero
temperatures (À208C) led to reactor clogging. Screening of
organic co-solvents further revealed an increase in yield by
conducting the reaction with 2-MeTHF at 08C (Table 1,
entry 5–7, Table S3). The stoichiometry of reagents was also
optimized as shown in Table 1 (entry 8–10) and Table S4. Two
[18]
relevant compounds.
Although different methods have
been reported for the synthesis of gem-difluoroalkenes,
[
19]
[20]
including Suzuki coupling, Negishi coupling, and Julia–
[
21]
Kocienski olefination, the Wittig-type reaction has received
considerable attention recently due to its straightforward
[
15a,22]
synthetic protocol.
ClCF H releases singlet difluorocar-
2
benes (DCF ) in the presence of base through deprotonation
2
[15b]
and a-elimination,
in which it is expected to be subse-
equiv of LiOt-Bu and 3 equiv of ClCF H was found to provide
2
quently trapped by triphenylphosphine to form a difluoro-
the best GC-FID yield of 82% at t (residence time) = 12 min
R
methyl triphenylphosphonium ylide (Ph P=CF ) for the
Wittig reaction with aldehydes. A model flow system for
(Table 1, entry 11). However, 1 was isolated in only 20% yield
3
2
[22]
after column chromatography while addition of water or D O
2
optimization was established as depicted in Table 1. ClCF H
to the crude reaction mixture would afford the corresponding
hydration products 2 and 3 (Scheme 1).
2
was infused into the system through an MFC (mass flow
controller) and piperonal was chosen as a benchmarking
substrate. We envisioned that LiOt-Bu (1m in THF) would be
a suitable base as it generates LiCl upon deprotonation and a-
elimination of the chlorodifluoromethyl anion, thus ensuring
a homogeneous mixture in THF. A BPR (back pressure
regulator) set at 50 psi effectively pressurized the system and
In the presence of stoichiometric amounts of triphenyl-
phosphine, we initially postulated a phosphine-catalyzed
hydration of the gem-difluoroalkenes which would resemble
the hydration of activated olefins reported by Bergman and
[
24]
Toste. Nonetheless, control experiments in which pure gem-
difluoroalkene 4 was treated with PPh under similar basic
3
enabled complete dissolution of ClCF H in the mixture.
Initial solvent screening showed that THF was a promising
candidate (Table S1), giving the gem-difluoroalkene product
conditions gave no hydration products (Table S5). Additional
experiments also excluded the possibility of side products in
this reaction serving as the active catalyst. We further carried
out a crossover experiment whereby gem-difluoroalkene 4
was subjected to the fresh crude mixture A from the flow
reaction and subsequently quenched with water (Scheme 2a).
Interestingly, only compound 2 was provided in 72% yield
while gem-difluoroalkene 4 did not undergo the hydration.
These results indicated that the former reaction halted at an
intermediate state which reacted with water to afford the a-
2
1
in 47% GC-FID yield (Table 1, entry 1). LiOMe in MeOH
was not compatible with the reaction (Table S1, entry 10)
while the use of KOt-Bu immediately clogged the micro-
reactor and mixers due to undissolved KCl (Table S1,
entry 11). The ylide (Ph P=CF ) was reported to be a transient
3
2
species in an interconversion between the ylide and difluor-
[22b,d]
ocarbene due to its low dissociation energy barrier.
While
Angew. Chem. Int. Ed. 2020, 59, 2 – 8
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