10.1002/cctc.201800754
ChemCatChem
FULL PAPER
*III/II
and lowest E1/2
(+0.66 V). The other catalysts are less
improved reproducibility, and automatized operation. The
efficient, requiring higher E1/2III/II and E1/2*III/II energies. This is
in line with the experimental results in the previous section.
A similar analysis can be derived based on the electronic
properties induced by the substituents on the brominated
arenes. With substituents having acceptor (-CO2H, -
CO2R, -CHO, -COR, -CF3, -CCl3), weak donor (-CH3, -R),
reactions
were
optimized
using
high-throughput
methodologies and generalized to a variety of starting
materials, demonstrating a wide functional group tolerance.
The reactivity differences among the substrates were
correlated with the steps of the reaction mechanism and with
the redox properties of the catalysts, deriving key catalyst
structure-performance relationships that can drive the design
of better and improved catalysts. We expect that the flow
photocatalytic methods described herein will find widespread
applications in academic and industrial labs for the synthesis
of pharmaceutical and agrochemical intermediates.
and acceptor and weak donor (-F, -Cl, -Br, -I)
III/II
properties, a photocatalyst with low E1/2 properties (cat1
)
and a non-nucleophilic base (e.g., DBU, pKa,DMSO = 12) is
required. With open amino acids and strong donors (-OH,
-OR in meta position), a milder catalyst (cat2) and a stronger
base (K3PO4 or Cs2CO3, pKa,DMSO = 12.6) are recommended.
For reactions involving nitriles, instead, an oxidizing
photocatalyst is needed to complete the catalytic cycle, since
the iridium is being oxidized from IrIII to *IrIV (Figure 8). The
highest photocatalytic activity in terms of oxidation potential
Experimental Section
General Procedure. Liquid chromatography-mass spectrometry (LC-MS)
analyses were performed with an analytical Agilent G4220A pump coupled
with Thermo MSQ Plus mass spectrometer (ionization: ESI+), Dionex
DAD-3000RS, evaporative light scattering detector (ELSD) Sedex 90,
using the Water (2.1 mm×50 mm, 2.5 µm) column from Agilent
Technologies. 1H nuclear magnetic resonance spectra were recorded at
room temperature on a Bruker NMR 500 MHz spectrometer equipped with
a DCH cryoprobe. Chemical shift () values are reported in parts per million
(ppm) downfield using the residual solvent signals as internal reference.
The multiplicity is described as singlet (s), doublet (d), and multiplet (m).
is obtained with cat5, which exhibits the lowest transition
IV/*III
energy for oxidation, E1/2
(-1.67 V), in line with the
experimental results. In all cases, the position of the leaving
group on the aromatic moiety of the brominated arene can
play a key role in the reaction: while para- and meta-positions
are tolerated, substituents in ortho-position could result in an
activity drop, likely due to steric hindrance effects. This is well
visible in Figure 6, where the yield of purified 6g is much
lower than that of 6j
.
It is important to highlight that the compounds depicted in
Figure 6 and Figure 7 are all formed as racemic mixtures.
This does not change in the presence of chiral ligands for the
Photocatalyst, base, and ligand screening (batch mode). In order to
investigate the performance of the different catalysts and bases, the
HepatoChem photochemical kits were used. This enables to conveniently
screen multiple reaction conditions simultaneously using pre-weighed
catalysts and reagents. Prior to the batch reaction, DMA was degassed in
N2. The aryl derivative (0.2 mmol) and the carboxylic acid (0.3 mmol) were
then dissolved in DMA (2 mL). A fraction of this stock solution (0.1 mL)
was transferred to each reaction vial containing the catalyst and the
reagents. The kit was then irradiated under visible light conditions ( = 430
nm) at 25°C for 16 h. Afterwards, an aliquot of the reaction product was
analyzed by liquid chromatography. Conversions were calculated with
LC/MS analyses and based on the following formula: Area products / (Area
starting material still present + Area products).
Ni-catalyzed cross coupling cycle.25 As shown in Figure S3
,
in fact, racemic products are formed in the presence of chiral
ligands as well. This is correlated with the mechanism in
Figure 8. After decarboxylation of 8c to 8d and CO2
extrusion, the stereochemical information in fragment 8d is
lost, resulting in a racemic mixture of products.
Scale-up synthesis. To finally demonstrate the scalability of
the flow method developed, the synthesis of compound 6h
was scaled up, producing 3.7 g of product within 8 h, with a
1
purified yield of 77% (100% pure by LC-MS and H-NMR).
Photocatalytic reactions (flow mode). Prior to the reaction, DMA was
degassed in N2. Typically, the aryl derivative (0.2 mmol), the carboxylic
acid (0.3 mmol), NiCl2.glyme (0.02 mmol), 4,4'-Di-tert-butyl-2,2'-dipyridyl
(0.03 mmol), and cat1 or cat2 (0.002 mmol) were dissolved in anhydrous
DMA (2 mL). Afterwards, DBU or K3PO4 (0.3 mmol) was added. For
decarboxylative arylations involving nitriles, the nitrile aryl substrate (0.2
mmol), the carboxylic acid (0.6 mmol), cesium fluoride (0.6 mmol), and
cat5 (0.004 mmol) were dissolved in anhydrous DMA (10 mL) and
deionized water (0.2 mL). In all cases, the resulting solution was stirred at
room temperature until complete dissolution of the solids, and degassed
with N2 for 20 min. The reaction was conducted on the reactor shown in
Figure 3. The solution, in particular, was injected in the photoreactor (10
mL internal volume) at T = 30-60°C, P = 1 bar, and F(mixture) = 0.2-2
mL/min, corresponding to a residence time, of 5-50 min. Isolation of the
product and recovery of the catalyst are more complicated in
This further confirms the benefits of using a continuous flow
microreactor to have predictable reaction scale-ups and the
possibility of a machine-assisted 24/7 working regime.
Conclusions
We have developed one-pot continuous processes to
construct photocatalytically a wide variety of
substituted benzylamines from cheap and readily available
-amino acids. Compared to traditional batch chemistry, the
-mono and di-
use of a flow photoreactor enables to overcome typical
photochemistry issues, such as non-uniform irradiation,
leading to quicker reactions (30 min instead of 12-72 h),
more predictable scale-ups, decreased safety hazards,
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