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Rapid Optimization of Photoredox Reactions for Continuous-Flow Systems Using Microscale Batch Technology

Photoredox catalysis has emerged as a powerful and versatile platform for the synthesis of complex molecules. While photocatalysis is already broadly used in small-scale batch chemistry across the pharmaceutical sector, recent efforts have focused on performing these transformations in process chemistry due to the inherent challenges of batch photocatalysis on scale. However, translating optimized batch conditions to flow setups is challenging, and a general approach that is rapid, convenient, and inexpensive remains largely elusive. Herein, we report the development of a new approach that uses a microscale high-throughput experimentation (HTE) platform to identify optimal reaction conditions that can be directly translated to flow systems. A key design point is to simulate the flow-vessel pathway within a microscale reaction plate, which enables the rapid identification of optimal flow reaction conditions using only a small number of simultaneous experiments. This approach has been validated against a range of widely used photoredox reactions and, importantly, was found to translate accurately to several commercial flow reactors. We expect that the generality and operational efficiency of this new HTE approach to photocatalysis will allow rapid identification of numerous flow protocols for scale.


■ INTRODUCTION
The past decade has witnessed exponential growth in the development of photoredox catalytic methods for organic synthesis. Photocatalysis, in which photon-harvesting molecules convert light energy to chemical energy, offers many useful advantages. In addition to being ecofriendly and sustainable, 1,2 photocatalytic methods are uniquely capable of promoting challenging bond formations 34 and novel chemical transformations 5−7 due to their ability to access high-energy intermediates in a controlled and selective manner. Photoredox catalysis is now used in the synthesis of agrochemicals, fine chemical intermediates, active pharmaceutical compounds (APIs), and finished dosage forms (FDFs). 8 While photocatalytic methods have found increasing industrial application, one remaining hurdle to widespread adoption of this platform is the inherent complexity in adapting photochemical reactions to large-scale settings, such as those required for process chemistry. 9−13 A critical outcome of the Beer−Lambert Law, with respect to the scale-up of photochemical transformations, is that photon-flux penetration decreases exponentially with depth in a given reaction medium, ultimately leading to attenuation in the transfer of photons. 14 Thus, visible-lightmediated reactions take place only in the proximal area (within 2 mm) of the vessel wall. 15−17 As such, a decrease in the diameter of the reaction vessel should lead to an increase in photon flux throughout the reaction medium and improved reaction efficiency. This observation has inspired recent efforts to develop (i) laser-based reaction platforms that employ highintensity photon sources, which in combination with continuous stirred tank reactors (CSTRs) provide powerful improvements with respect to photon penetration in a batchflow setting, and (ii) continuous-flow photoreactors, which naturally permit better light penetration due to the narrow tubing diameter; such systems have been shown to permit gram-and kilogram-scale transformations. 18,19 In general, flow reactor platforms offer many advantages over batch chemistry 20−26 with respect to photon efficiency, reproducibility, scale-up, safety, waste generation, and productivity regarding both yield and reaction time (Figure 1a). Along these lines, a number of research groups have adopted flow photochemistry strategies for the synthesis of molecules of pharmaceutical interest (Figure 1b). 27−29 Despite these advantages, the optimization of a flow chemistry process typically can be an onerous task for several reasons: (i) it is traditionally not possible to perform parallel optimization experiments in the context of a flow system; (ii) the optimal reaction conditions are highly dependent on the size of the individual reactor; and (iii) each flow chemistry experiment requires significant amounts of material compared to the analogous reaction conducted in batch. 30,31 A number of strategies have been pursued to streamline optimization of flow-based photoredox methods, including reducing the reaction vessel size, 32−37 leveraging mathematical equations 38 and algorithms, 36,39,40 and adapting new technologies (segmented 41,42 or microflow 43−46 and industry 4.0 47 ).
Over the past decade, high-throughput experimentation (HTE) methodologies have been successfully employed in the optimization of numerous catalytic transformations. 48−51 Such technology has been adopted within both academic and industrial settings to allow the evaluation of reaction parameters while minimizing economic and waste constraints. Recently, the optimization of photoredox protocols has also been conducted using HTE technology. 34,35 Using such strategies, it has been possible to build foundational results from which reaction optimization can be examined thereafter in continuous-flow systems. However, a limitation of existing optimization platforms is the difficulty in translating HTE outcomes to continuous-flow platforms, a feature that often relates to the change in vessel, light intensity, and light pathlength considerations. 49,51−55 A complementary approach was beautifully described by the Stephenson group 56 at the outset of the preparation of this manuscript, demonstrating a flowbased HTE platform by developing a droplet microfluidic system for the development of photochemical reactions. This study is focused on the generation of compound libraries, ultimately increasing the chemical space with great time and material efficiency. Notwithstanding, to the best of our knowledge, a general HTE strategy for the translation of optimized photoredox reactions seamlessly to similar outcomes on a flow platform remains undeveloped and would be of a great interest to both discovery programs and process chemistry alike.
With this in mind, we sought to design an HTE platform that mimics the conditions of a flow reactor. 48−55 A requisite goal would be that the optimization data collected via this HTE platform should be directly transferrable to a flow system, permitting the rapid translation of small-scale batch-vessel photoredox reactions to large-scale flow systems. Thus, the HTE setup should allow us to perform miniaturized reactions while simulating continuous photonic flow chemistry protocols.
A compelling benefit of such a system is the ability to simultaneously explore numerous reaction variables, including the catalyst, photon intensity, base, solvent, and so on, in parallel while employing short residence times. We describe herein the development of this HTE platform and its validation in the context of four representative photoredox transformations.

■ FLOSIM PLATFORM DESIGN
Design Plan of an HTE Platform to Simulate Continuous-Flow Systems. Successfully modeling photochemical flow reactions in a high-throughput setting requires designing a system that adequately captures the distribution of photonic energy present throughout the entire protocol employed within the flow apparatus. 57,58 In a photoredox-catalyzed transformation, wherein the approximations of the Beer−Lambert law operate, the photon absorption is described as a function of the incident radiation and the absorption coefficient. 59 Given the angular and spatial dependence of the spectral specific intensity and the complex geometric considerations required to accurately describe irradiation in flow, we recognized that determining the specific spectral intensity to enable design of a corresponding highthroughput setup would prove to be challenging at best. Importantly, however, we recognized that the key components of spectral intensity could be appropriately accounted for by selection of a light source that results in the same radiant flux for both systems. 60 Furthermore, the incident radiation could now be approximated by ensuring the same path length of irradiation under both flow and high-throughput batch conditions. With this in mid, we sought to accomplish a path-length matching feature by the operationally simple step of varying the volume in a standard 96-well plate to generate a solution height matching the internal diameter (ID) of the transparent fluorinated ethylene propylene (FEP) tubing Next, in order to simulate the flow-system environment in the context of a photochemical reaction, it would be crucial to recreate the reactor-coil element. Accordingly, we assembled a multienvironment 96-well plate glass device that enables a high level of light exposure (Figure 2b). This platform was equipped with two Kessil LEDs (PR160) and two ThorLabs concave lenses (see Supporting Information for details), while temperature control was maintained through air convection methods. The use of a glass 96-well plate allows complete penetration and reflection of the light inside the device in all directions, and the uniformity of photon dispersion is accomplished across the platform using a ThorLabs concave lens and several highdensity reflection mirrors.
In order to evaluate the system's ability to facilitate photoredox reactions with satisfactory consistency within the plate, we conducted a series of simple test reactions using different materials at different positions along the plate (see Supporting Information). 61 In Figure 2c, we outline the general workflow for the translation of a photoredox reaction from batch to flow using a multiscreening platform. Route scouting to identify optimal reaction conditions begins with validation of the reaction, in batch, across different wavelengths. Next, reaction optimization is performed on microscale using the flow simulation (FLOSIM) HTE setup. Briefly, the 96-well glass plate is loaded inside a nitrogen-filled glovebox, sealed with transparent film, and placed in the benchtop HTE device, where it is exposed to light irradiation for a short period of time equivalent to the desired residence time in the flow system. Following completion of screening, the crude reaction mixtures are analyzed by ultraperformance liquid chromatography (UPLC). This two-step process, HTE screening of different conditions, and analysis of results via UPLC, can be performed iteratively until the desired results are obtained.
Last, the optimal conditions, as determined from the HTE microscale platform, were directly reproduced in the commercial flow system using the preferred wavelength, light intensity, substrate/reagent concentrations, residence time, solvent, base, and so on. As described below, the optimized conditions identified at the 60 μL scale in the glass plate system were found to be directly transferrable to a UV-150 Vapourtec E-Series system equipped with a 2 mL or 10 mL reactor coil. We have demonstrated the utility and generality of this FLOSIM HTE optimization protocol in the context of four representative photocatalytic reactions widely employed in medicinal chemistry.

■ RESULTS AND DISCUSSION
Optimization of Decarboxylative Arylation for Flow. In 2014, we reported a novel decarboxylative arylation, 62 wherein amino acids are transformed into benzylic amines under synergistic photoredox and nickel catalysis (Figure 3a). In optimizing this transformation for a flow system, we selected N-Boc-Proline (Boc-Pro-OH) and 1-bromo-4-(trifluoromethyl)-benzene as model substrates. We first validated the reaction using a bench setup: under published conditions with a 26 W CFL light bulb and Cs 2 CO 3 base, the desired product was isolated in 88% yield after 36 h. We began optimization studies by evaluating the efficiency of the decarboxylative arylation across a variety of wavelengths (PR160 Kessil LEDs); these investigations revealed 427 nm to be the optimal wavelength for the transformation. An important consideration in developing flow reactions is the need to avoid heterogeneous conditions, 63−65 which often clog the tubular flow reactors. With this criterion in mind, we set out to optimize the transformation using the HTE FLOSIM−UPLC setup, with an eye toward identifying suitable organic bases and solvents to ensure a homogeneous solution (see Supporting Information). Approximately 300 "flow-type" reaction conditions were tested in short order to examine the effect of residence time, solvent, concentration, organic base, photocatalyst, catalyst loading, as well as the nature of the transition metal complex (see Supporting Information). As shown in Figure 3b, these studies led to the identification of homogeneous conditions that afforded the desired transformation in only 45 min with 79% yield. We next sought to transfer these conditions to a flow platform: a UV-150 Vapourtec E-Series system equipped with a 2 mL reactor coil and 420 nm LED. We were pleased to find that the HTE-optimized reaction conditions were directly Figure 2. Simulation process and sequential optimization method. (a) By using the inner diameter of the reactor-coil tubing as the height on the plate, we can calculate the required reaction volume. (b) To simulate the flow reactor, a reflected FLOSIM device was built and validated across various parameters, such as the position, lights, and cooling system. The FLOSIM device was optimized to obtain both high reactivity in conjunction with homogeneity across the plate. (c) Workflow: Selection of the optimal wavelength for the reaction is followed by optimization in the 96-well glass plate FLOSIM device. After the reaction, the sample is diluted and analyzed by UPLC. The selected conditions are then validated through transfer into the commercial flow system. translatable to the Vapourtec, delivering the desired product with comparable levels of efficiency (74% yield) using the same conditions including 45 min of residence time (Figure 3b). In order to be confident that the HTE platform offers an accurate simulation of the Vapourtec flow system, we sought to determine the consistency of data between both systems using a variety of reaction conditions. As shown in Figure 3b, we selected two sets of conditions that gave mediocre and poor results respectively with the HTE setup (i.e., 50 and 7% yield). Indeed, when these suboptimal conditions were transferred to the Vapourtec reactor, we again found a remarkable level of consistency between the HTE FLOSIM batch reactors and the flow efficiencies (56 and 6% yield, respectively). These results suggest that the optimization data obtained in the context of the HTE platform are, indeed, indicative of performance in flow. Moreover, time studies conducted for both the HTE setup and the flow setup under optimal conditions reveal a strong correlation between the two systems with respect to conversion as a function of reaction time (see Supporting Information).
Next, we aimed to demonstrate the feasibility of this flowoptimized method in processes of different scale. As shown in Figure 3c, when the reaction was conducted at the 60 mmol level using the optimized conditions with a larger coil size reactor (10 mL), the desired product was isolated in 70% yield. Moreover, 13.2 g of product was isolated after an 11.7 h total flow reactor time using the Vapourtec system. In comparison to the laboratory vial reactor procedure, which provides 111 mg of desired product in 36 h, we were able to demonstrate a 366-fold increase in efficiency by way of this rapid, flow optimization protocol.
Optimization of C−N Arylation Coupling for Flow. In 2018, our group reported a new transformation that allows the decarboxylative alkylation of N-nucleophiles via the merger of photoredox and copper catalysis. 66 Among a large scope of valuable alkylation substrates, there has been growing interest in the incorporation of rigid bicyclic structures, such as [1.1.1]propellane (BCP) scaffolds, into medicinal compounds, owing to their capacity to act as bioisosteres of alkynes or parasubstituted benzene rings. With this consideration in mind, we sought to optimize a flow method for the rapid production of molecules containing the BCP scaffold via our C−N coupling platform. We selected 3-(methoxycarbonyl)bicyclo[1.1.1]pentane-1-carboxylic acid and 3-chloro-indazole as the model coupling partners. Using our previously published conditions, the C−N coupling adduct was obtained in a vial batch in 80% yield after 1 h. After a subsequent survey of reaction efficiencies as a function of LED wavelength, it became apparent that the coupling proceeds well across a variety of light sources, and 390 nm was selected for further HTE studies (see Supporting Information). As shown in Figure 3e, following a short HTE FLOSIM−UPLC optimization campaign that involved the assessment of ∼300 reactions (evaluating different reaction times, solvents, concentrations, catalysts and catalyst loadings, see Supporting Information), we identified optimal flow conditions that provided comparable efficiency (89% yield) within only an 8 min reaction time.
These conditions were then directly transferred to the continuous-flow system (Vapourtec E-Series, 2 mL reactor coil), and a similar result was obtained (87% yield, 8 min residence time). As shown in Figure 3e, a time study showed comparable levels of conversion between the HTE and commercial flow setups for a variety of conditions that were examined, lending further support to the predictive power of the HTE setup (Figure 3e).
Finally, the decarboxylative alkylation was performed on a 40 mmol scale using our optimized FLOSIM conditions on a Vapourtec reactor (385 nm LEDs, 10 mL reactor coil). The reaction was conducted in the heated mode at 35°C to prevent solvent freezing. Under the conditions shown in Figure  3f, 7.6 g of the desired product was isolated in good yield (69%) after only 10 h, representing a 6.5-fold increase in reaction efficiency over the vial batch setup.
Optimization of Cross-Electrophile Coupling for Flow. In 2016, we developed a cross-electrophile coupling that has found broad application across a variety of medicinal chemistry campaigns. 67 As such, the development of a simple protocol by which to translate small-scale cross-electrophile couplings to commercial flow systems would have significant benefit for the scale-up of critical building blocks and drug-like fragments or products. Under our standard vial batch setup, the model substrates, 4-bromotetrahydropyran and methyl-4bromobenzoate, underwent cross-coupling to afford the desired product in 79% yield over the course of 6 h. Moreover, irradiation at 427 nm was observed to be optimal for this transformation (see Supporting Information). Given that HBr is generated as the main byproduct in this coupling protocol, 17 we undertook an evaluation of various soluble organic bases. While initial FLOSIM studies revealed that 2,6-lutidine appeared to be an effective acid scavenger and compatible with high coupling yields, the resulting side product, a lutidinium bromide salt, has poor solubility and ultimately causes the flow system to clog. As such, we were unable to translate this initial set of HTE-optimized conditions beyond an 8 mmol scale using the commercial flow reactor (Figure 4c; also see Supporting Information) due to the need to incorporate frequent wash cycles to remove salt byproducts.
Given the broad interest in this coupling protocol across the industrial sector, 68−70 we undertook a second optimization campaign using the HTE FLOSIM device, with the goal of identifying homogeneous conditions that would provide improved properties for scale-up. In this regard, we performed approximately 1000 experiments via HTE FLOSIM to evaluate a variety of reaction components (bases, solvents, concentrations, reaction times, metal complexes, catalyst loadings, additives, and cosolvents; see Supporting Information). Through this process, we determined that (i) decreasing the amount of base from 2 to 1 equiv, (ii) switching to a more polar solvent [N,N-dimethylacetamide (DMA)], and (iii) extending the reaction time to 45 min provided optimal efficiency without issues related to salt precipitates. Moreover, with these conditions in hand, we were able to achieve high efficiency in both the HTE setup (77% yield) and the commercial flow system (77% yield) (Figure 4d). Most importantly, as shown in Figure 4d, we were able to scale this reaction to 60 mmol using the Vapourtec E-Series (10 mL reactor coil and 420 nm LEDs) to obtain 10.3 g of the coupled product in 78% yield after 23 h.
In comparison to the initial vial batch protocol (87 mg obtained), this result represents a 30.9-fold improvement in efficiency.
Optimization of Visible-Light-Mediated C−O Arylation Coupling for Flow. Our photocatalytic C−O coupling reaction 71 has emerged as a versatile strategy for the synthesis of alkyl aryl ethers. Under the standard bench setup, using a relatively complex protected pyranose model substrate and an aryl bromide, the etherification generated the desired product in 82% yield after 24 h. Irradiation at 456 nm was found to provide optimal reaction efficiency (see Supporting Information). Optimization studies with the HTE FLOSIM platform (∼450 experiments to evaluate all the components in the reaction, see Supporting Information) revealed the inexpensive organic photocatalyst, 2,4,5,6-tetra(9H-carbazol-9-yl)isophthalonitrile (4CzIPN), to be the ideal catalyst, generating the coupling product in 80% yield after 35 min (Figure 5b). Translating these optimal HTE conditions to the commercial flow system yielded similar results (75% yield), and time studies demonstrated a strong correlation between these two platforms. Once again, the results generated from the HTE system were consistent with those obtained from the flow system across a variety of optimal and nonoptimal conditions (Figure 5b).
Translation of the HTE FLOSIM Platform to Multiple Commercial Flow Reactors. Throughout most of this project, we employed a UV-150 Vapourtec E-Series as a representative flow reactor for scale-up. In order to With the workflow shown using 456 nm Kessil LEDs, followed by HTE optimization and the corresponding UPLC analysis, we could obtain in a flow system the desired product (75% yield) in 35 min of residence time instead 24 h of reaction time using a standard setup. Optimization using our HTE protocol provides a range of conditions, which we could translate successfully to the flow system. (c) The efficiency of our protocol was also proved by using a powerful continuous-flow system (PhotoSyn). Using the 25% light intensity, we could observe a correlated result with our HTE setup. Furthermore, increasing the light intensity, we were able to reduce the reaction time with no changes on the reactivity. (d) The effectivity of this reaction has been proved for both continuous-flow systems affording the same reactivity (72% yield), resulting in a higher efficiency for the more powerful flow system (26.6 g/day for Vapourtec and 56.3 g/day using PhotoSyn. demonstrate the generality of this approach for practitioners in this field, we sought to test our protocol in a second, commercial flow system. In this context, we evaluated the PhotoSyn flow photoreactor as developed and manufactured by Uniqsis Ltd. This photoreactor is equipped with a 10 mL reactor coil (ID = 1.0 mm) and more powerful LEDs (455 nm LEDs, 700 W total power, approximately 200 W output power) compared to the Vapourtec system. According to literature precedent, 33 flow reactors that incorporate highpowered photonic sources may offer numerous benefits, including faster reaction rates, shorter reaction times, and amenability to nonhomogeneous conditions. On this basis, we evaluated the efficiency of the above-mentioned C−O coupling protocol in the PhotoSyn flow system using various light intensities as determined via our HTE FLOSIM platform. As shown in Figure 5c, using 25% light intensity, we were able to achieve satisfactory yield (76% yield in HTE FLOSIM vs 79% in PhotoSyn) with a residence time of 35 min. Moreover, by increasing the light intensity to 75%, we obtained a comparable 79% yield with a much shorter reaction time of 13.75 min (Figure 5c, also see Supporting Information). Finally, we attempted a gram-scale synthesis of the product with each continuous-flow system (Figure 5d). Under optimized conditions, the Vapourtec system provided 12.2 g of final product in 11 h (72% yield), while the PhotoSyn system is able to generate 26.2 g of the same product in the same time frame (72% yield). Thus, compared to a batch setup, which provides 310 mg of product in 24 h, the flow system can lead to an 86fold efficiency acceleration using the Vapourtec system and 185-fold efficiency enhancement using the PhotoSyn photoreactor. More importantly, we have demonstrated that our HTE FLOSIM optimization strategy can be applied across various commercial flow reactors.

■ CONCLUSION
In summary, we have designed an HTE FLOSIM device that can simulate a continuous-flow setup to enable the optimization and direct translation of small-scale photoredox methods to large-scale flow reactors. This system permits the reproduction of the same reaction pathways in both an HTE setup and a continuous-flow setup and therefore serves as a general platform to rapidly optimize any photoredox reaction at microscale. We have evaluated this optimization platform in the context of four prominent photocatalytic transformations, and in each case, we have been able to significantly improve the efficiency of these methodologies at large scale compared to standard batch conditions. Moreover, the generality of this platform with regard to different flow reactors has been demonstrated. Considering the widespread interest in photoredox catalysis across the pharmaceutical industry, we expect this optimization platform to be widely adopted in both medicinal and process chemistry settings.