Angewandte
Communications
Chemie
tions is continuous flow.[16] Owing to decreased path lengths
be achieved safely and controllably. Additionally, the assem-
and increased interfacial area, mass- and energy-transfer rates
are significantly enhanced in such systems, often providing
superior results relative to batch reactions.[17] The ability to
precisely control reaction conditions can also improve scal-
ability and safety.
bled setup (2.7 mL in volume) was capable of almost five
times the material throughout (0.19 mmol product/h vs.
0.04 mmol/h in batch).
We also carried out preliminary investigations of the
mechanism of this transformation. In particular, we looked to
À
To examine these advantages with regard to the devel-
oped methodology, a simple flow setup was assembled
(Scheme 2A). Within it, substrate, catalyst, and reductant
are pumped as a single stream and then combined with
gaseous SF6 via a Y-mixer (M1). The flow rate of SF6 is
adjusted to create a uniform 1:1 gas:liquid segmented (“slug”)
flow in the reaction line. Prior to irradiation, the two phases
mix in R1 (residence time: tR = 1 min) before entering R2 (tR =
15 min), which is illuminated by blue LEDs. Following the
reaction, a back-pressure regulator (BPR) is used to place the
entire system under 100 psi of pressure and increase the
solubility of SF6 in solution.
gain better understanding of the nature of C F bond
À
formation. Prior to C O bond cleavage, we anticipated that
the alcohol would likely attack the sulfur atom of some SFx
species, since a similar step has been proposed for other
sulfur-based deoxyfluorination reagents. As would be
expected based on this proposal, when oxygen was protected
(27), no reactivity was observed (Scheme 3). Furthermore, the
À
formation of an O S bond is supported by a dialkyl sulfite
side product[13] observed in small quantities under the
reaction conditions.
Under the optimized conditions, 6 was furnished in 79%
yield relative to conversion of starting material, with a total
residence time of 16 min, as compared to a 55% yield
obtained in 14 h in batch (entries 1 and 3 in Scheme 2).
Similar improvements were also observed for 11 and 12
(Scheme 2B). Interestingly, in continuous flow, starting
material is consumed within 2 min, generating the desired
products as well as a previously unobserved intermediate,
most consistent with (RO)2SF4. Over the course of the
reaction, this intermediate is gradually converted back into
starting material, preventing undesired side reactions. Given
that elevated pressure (100 psi) did not produce similar
conversions and yields in batch, it is likely that the increased
pressure, mass-transfer, and interfacial area of the continu-
ous-flow system all contribute to the formation of the
intermediate and the improved yield-to-conversion ratio.
Also noteworthy are the safety and throughput enabled under
continuous flow. In the system, SF6 can be easily handled with
use of a BPR, allowing for the elevated pressures utilized to
Scheme 3. Standard conditions (std. cond.): SF6, Ir(ppy)2(dtbbpy)PF6
(5 mol%), DIPEA (3 equiv), DCE (0.075m), irradiation with blue LEDs,
room temperature, 14 h. Linear:branched (l:b) ratio determined by
NMR spectroscopic analysis.
À
We further hypothesized that C O bond cleavage could
occur via a one- or two-electron process. The addition of one
equivalent of TEMPO, however, had little effect on the
reaction, giving a 47% yield (1.4:1 l:b) of 6 compared to 55%
yield obtained in its absence. Additionally, no evidence for
the formation of TEMPO adducts was observed in these
reactions suggesting the absence of fluorine radicals and
sufficiently long-lived radical intermediates of the starting
À
material. The two-electron nature of C F bond formation was
further supported by radical clock experiments (Scheme 3). If
during the course of the reaction an allylic radical is generated
À
via C O bond homolysis, a 5-exo-trig cyclization or radical
cyclopropane ring opening would be expected to occur for
substrates 28 and 31, respectively. However, neither 30 nor 33
were observed (Scheme 3).
Although further studies are necessary to reveal mecha-
nistic details, preliminary experiments indicate that the
mechanism of this deoxyfluorination may share features
with that of the chlorination of alcohols with thionyl chloride.
À
À
In this case, C O bond cleavage precedes C X bond
formation from an undissociated ion pair. As noted, the
formation of both ammonium salts and Ritter-type products
derived from the allylic alcohol were observed, suggesting the
presence of an intermediate with significant cationic charac-
ter. Furthermore, deoxyfluorination of trans and cis-(À)-
carveol proceeded with overall retention of stereochemistry
Scheme 2. Continuous-flow deoxyfluorination. [a] Determined by
1H NMR with dimethyldiphenylsilane as an internal standard. [b] Yield
relative to conversion of starting material.
Angew. Chem. Int. Ed. 2016, 55, 1 – 5
ꢀ 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
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