Abstract:The synthesis of many valuable C19 androgens can be accomplished by removal of the C17 side chain from more abundant corticosteroids, followed by further derivatization of the resulting 17‐keto derivative. Conventional chemical reagents pose significant drawbacks for this synthetic strategy, as large amounts of waste are generated, and quenching of the reaction mixture and purification of the 17‐ketosteroid intermediate are typically required. Herein, we present mild, safe, and sustainable electrochemical stra… Show more
“…13 C NMR (125 MHz, chloroform-d): δ 216.8, 207.6, 199.5, 167.9, 124.8, 63.3, 50.4, 50.4, 49.8, 38.3, 36.3, 35.9, 34.7, 33.7, 31.9, 30.9, 21.6, 17.3, 14.7 ppm. These data agree with those previously reported in the literature …”
Section: Methodssupporting
confidence: 94%
“…Then, the solvent was evaporated under reduced pressure and the residue was diluted with aqueous NaHCO 3 (sat) and extracted with DCM. The organic phase was dried over Na 2 SO 4 and evaporated under reduced pressure, yielding 141.4 g (94%) of adrenosterone ( 6 ) as an off-white solid, mp 204–205 °C (lit . 206–208 °C).…”
Section: Methodsmentioning
confidence: 99%
“…The organic phase was dried over Na 2 SO 4 and evaporated under reduced pressure, yielding 163.5 g (91%) of adrenosterone ( 6) as an off-white solid, mp 201−202 °C (lit. 24…”
Technology for the rapid scale-up of synthetic organic
electrochemistry
from milligrams to multigrams or multi-100 g quantities is highly
desirable. Traditional parallel plate flow electrolysis cells can
produce large quantities of material, but transfer from batch to this
flow technology requires reoptimization of the reaction conditions
and fully homogeneous reaction mixtures. Moreover, single-pass processing
is often difficult to accomplish due to gas generation and the low
flow rates typically used in continuous mode. Herein we present a
novel reactor design, based on a rotating cylinder electrode concept,
that enables seamless scale up from small scale batch experimentation
to gram and even multikilogram per day quantities. The device can
operate in batch and flow mode, and it is able to easily process slurries
without clogging of the system or fouling of the electrodes. Continuous
operation is also demonstrated using three reactors in series that
act as a continuous stirred electrochemical reactor cascade, providing
kilogram per day productivities in a single pass.
“…13 C NMR (125 MHz, chloroform-d): δ 216.8, 207.6, 199.5, 167.9, 124.8, 63.3, 50.4, 50.4, 49.8, 38.3, 36.3, 35.9, 34.7, 33.7, 31.9, 30.9, 21.6, 17.3, 14.7 ppm. These data agree with those previously reported in the literature …”
Section: Methodssupporting
confidence: 94%
“…Then, the solvent was evaporated under reduced pressure and the residue was diluted with aqueous NaHCO 3 (sat) and extracted with DCM. The organic phase was dried over Na 2 SO 4 and evaporated under reduced pressure, yielding 141.4 g (94%) of adrenosterone ( 6 ) as an off-white solid, mp 204–205 °C (lit . 206–208 °C).…”
Section: Methodsmentioning
confidence: 99%
“…The organic phase was dried over Na 2 SO 4 and evaporated under reduced pressure, yielding 163.5 g (91%) of adrenosterone ( 6) as an off-white solid, mp 201−202 °C (lit. 24…”
Technology for the rapid scale-up of synthetic organic
electrochemistry
from milligrams to multigrams or multi-100 g quantities is highly
desirable. Traditional parallel plate flow electrolysis cells can
produce large quantities of material, but transfer from batch to this
flow technology requires reoptimization of the reaction conditions
and fully homogeneous reaction mixtures. Moreover, single-pass processing
is often difficult to accomplish due to gas generation and the low
flow rates typically used in continuous mode. Herein we present a
novel reactor design, based on a rotating cylinder electrode concept,
that enables seamless scale up from small scale batch experimentation
to gram and even multikilogram per day quantities. The device can
operate in batch and flow mode, and it is able to easily process slurries
without clogging of the system or fouling of the electrodes. Continuous
operation is also demonstrated using three reactors in series that
act as a continuous stirred electrochemical reactor cascade, providing
kilogram per day productivities in a single pass.
“…Evidence for generating iminium intermediates was observed with 1 where N -demethylation was a major impurity, presumably formed via the process outlined in the Supporting Information. This N -demethylation is precedented in amine oxidation chemistry both under photoredox and electrochemical conditions, including aerobic Rh catalysis …”
Employment of a combination of an organophotoredox catalyst with Wilkinson's catalyst (Rh(PPh 3 ) 3 Cl) has given rise to an unprecedented method for hydrogen-isotope exchange (HIE) of aliphatic C(sp 3 )−H bonds of complex pharmaceuticals using T 2 gas directly. Wilkinson's catalyst, commonly used for catalytic hydrogenations, was exploited as a precatalyst for activation of D 2 or T 2 and hydrogen atom transfer. In this combined methodology and mechanistic study, we demonstrate that by coupling photocatalysis with Rh catalysis, carbon-centered radicals generated via photoredox catalysis can be intercepted by Rh-hydride intermediates to deliver an effective hydrogen atom donor for hydrogen-isotope labeling of complex molecules in one step. By optimizing the ratio of the photocatalyst and Wilkinson's catalyst to balance the rate of the dual catalytic cycles, we can achieve efficient HIE and high recovery yield. This protocol was readily applied to direct HIE of C(sp 3 )−H bonds in 10 complex drug molecules, showing high isotope incorporation efficiency and exceptionally good functional group tolerance and demonstrating this approach as a practical and attractive labeling method for deuteration and tritiation.
“…A mixture MeCN/H2O was used as solvent in both cases, with a concentration of 1a of 0.1 M. For the TEMPO-mediated oxidation, the water phase contained 0.1 M of a phosphate buffer of pH = 9.2, 5,16 which also acted as supporting electrolyte. As expected, when TEMPO was used as mediator, aldehyde 3a was observed as the major oxidation product (Figure 2).…”
Selective anodic oxidation of alcohols in the presence of other functional groups can be accomplished using nitroxyl radical mediators. However, the electrochemical chemoselective oxidation of secondary alcohols in the presence of primary alcohols is an unsolved issue. Herein, we report an electrochemical procedure for the selective oxidation of secondary alcohols using an inexpensive chloride salt that acts as redox mediator and supporting electrolyte. The method is based on the controlled anodic generation of active chlorine species, which selectively oxidize secondary alcohols to the corresponding ketones when primary hydroxyl groups are present. The method has been demonstrated for a variety of substrates. The corresponding ketones were obtained in good to excellent yields. Moreover, the chloride salt can be easily recovered and reutilized by a simple extraction procedure, rendering the method highly sustainable
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.