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Towards More Efficient, Greener Syntheses Through Flow Chemistry

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Towards More Efficient, Greener Syntheses Through Flow Chemistry Towards More Efficient, Greener Syntheses through Flow Chemistry The MIT Faculty has made this article openly available. Please share how this access benefits you. Your story matters. Citation Lummiss, Justin A.M. et al. “Towards More Efficient, Greener Syntheses through Flow Chemistry.” The Chemical Record 17, 7 (February 2017): 667–680 © 2017 Wiley-Verlag As Published https://doi.org/10.1002/tcr.201600139 Publisher Wiley Blackwell Version Author's final manuscript Citable link http://hdl.handle.net/1721.1/114543 Terms of Use Creative Commons Attribution-Noncommercial-Share Alike Detailed Terms http://creativecommons.org/licenses/by-nc-sa/4.0/ PERSONAL ACCOUNT Alternatively, entire flow systems with specialized attachments Towards More Efficient, can be purchased from various commercial suppliers.[4b] Greener Syntheses Through Flow Chemistry Justin A.M. Lummiss,[a] Peter D. Morse,[a] Rachel L. Beingessner,[a] and Timothy F. Jamison*[a] Abstract: Technological advances have an important role in the design of greener synthetic processes. In this Personal Account, we describe a wide range of thermal, photochemical, catalytic, and biphasic chemical transformations examined by our group. Each of these demonstrate how the merits of a continuous flow synthesis platform can align with some of the goals put forth by the Twelve Principles of Green Chemistry. In particular, we illustrate the potential for improved reaction efficiency in terms of atom economy, product yield and reaction rates, the ability to design synthetic process with chemical and solvent waste reduction in mind as well as highlight the benefits of the real- time monitoring capabilities in flow for highly controlled synthetic output. Figure 1. (a) Comparison of the major unit operations in batch relative to flow. (b) Additional tools utilized in flow reactions including a (left) mass flow controller (MFC), which is used to regulate gas flow and (right) check valves (CV), which are used to prevent back flow. 1. Introduction [1] First outlined by Anastas and Warner in 1998, the Twelve There are several benefits of flow chemistry compared to Principles of Green Chemistry provide a valuable framework for traditional batch synthesis.[3e, 5] For example, the high surface evaluating the efficiency and sustainability of a given chemical area to volume ratio of a flow reactor enables superior mixing of [2] transformation or process. On the molecular level, these biphasic reactions, such as those between gases and liquids, principles call for the design of reactions that are more atom which can significantly improve product yields.[5b] This same economical, minimize the use of hazardous reagents, and utilize attribute also permits precise temperature control, which can renewable feedstocks. The design of reaction protocols with increase reaction efficiency (e.g. reaction rate, product yield) energy efficiency in mind, and employing real-time reaction while minimizing energy consumption.[3d] Photochemical analysis in order to minimize waste generation are also among transformations can similarly benefit from improved yields, the recommendations. Technological advances, such as decreased reaction time-scales, and reduced catalyst loadings, continuous flow synthesis, have an important role to play in due to the highly efficient irradiation that results from having a [3] advancing these goals. short path length.[5d, 6] Continuous flow reactions on the meso- to macro-scale level Another distinguishing feature of continuous flow is that the are typically carried out within commercially available small amount of product generated is determined by the length of time diameter tubing (inner diameter 0.01-0.080”) fabricated from the entire flow regime is operated, given defined flow rates and either polymer (e.g. perfluoroalkoxy alkanes, Tefzel, reactor volumes. This is in contrast to batch, where the polyetheretherketone) or metal (e.g. stainless steel, copper) maximum quantity of product produced per reaction, is [4] materials. A range of Swagelok and HPLC fittings enable the predetermined by the quantity of starting material. It is this very relatively facile assembly of bespoke flow set-ups using some or nature of continuous production that enables small volume flow all of the components showcased in Figure 1a and b. reactors to produce comparably large quantities of product. The reduced reactor volume in flow also enables more efficient engineering controls and also inherently reduces safety risks by [a] Dr. J. A. M. Lummiss, Dr. P. D. Morse, Dr. R. L. Beingessner, avoiding large accumulations of potentially hazardous Professor T. F. Jamison intermediates at any given point in time. Department of Chemistry Massachusetts Institute of Technology 77 Massachusetts Avenue, Cambridge, MA, 02139, USA E-mail: [email protected] PERSONAL ACCOUNT A major research focus of our group lies in leveraging continuous flow platforms to improve reaction outcomes and Tim Jamison was born in San Jose, CA, and enable transformations that are difficult, or simply not feasible to grew up in neighboring Los Gatos, CA. He perform in batch.[7] In this Personal Account, we highlight several received his undergraduate education at UC of these reactions that also align with the goals outlined by the Berkeley, where he conducted research in Twelve Principles of Green Chemistry.[1] The examples the laboratory of Prof. Henry Rapoport for described are diverse in nature and include a number of thermal, nearly three years. He was then a Fulbright photochemical, catalytic and biphasic (e.g. gas-liquid) reactions. Scholar with Prof. Steven A. Benner at the While they have not been scrutinized with regards to their overall ETH Zurich, and thereafter he undertook his greenness, our aim is simply to illustrate how our goals for Ph.D. studies at Harvard University with improved reaction efficiency in terms atom economy, product Prof. Stuart L. Schreiber. He then moved to yields and reaction rates, offer opportunities within the context of the laboratory of Prof. Eric N. Jacobsen at green chemistry. We also aim to demonstrate the feasibility of Harvard University, where he was a Damon chemical and solvent waste reduction within a flow synthesis Runyon-Walter Winchell postdoctoral fellow. In 1999, he began his independent career at MIT, where he currently holds the positions of R. R. design as well as highlight the merits of real-time monitoring for Taylor Professor and Head of the Chemistry Department. maintaining the integrity of larger-scale production. Overall, our hope is that the reader considers the prospects of continuous flow as a stepping stone towards greener, more efficient syntheses. 2. Flow-Enabled Greener, More Efficient Syntheses Justin Lummiss received his Ph.D. in 2015 from the University of Ottawa, for work with 2.1. Thermal Reactions - Improved Product Yields and Deryn Fogg on mechanistic organometallic Reaction Rates, Efficient Heat Transfer Processes chemistry in olefin metathesis. He is presently an NSERC postdoctoral fellow A central pillar toward greener chemistry is the design of with Timothy Jamison at MIT. increasingly efficient syntheses. While reducing the volume of waste generated by reactions is the primary means for improving E-factors, additional aspects such as increasing the product yield, decreasing the reaction time, carrying out more atom economical transformations and minimizing energy loss all impact the overall efficiency of a synthesis. Peter Morse studied Structural Biology and One of the well-known benefits of continuous flow is the Chemistry at the University of Connecticut ability to safely heat a reaction mixture well beyond the boiling (B.S.). In 2010, he joined the lab of David point, by regulating the pressure of the system with a back Nicewicz as a graduate student at the pressure regulator shown in Figure 1a.[4b, 4c] While high University of North Carolina at Chapel Hill. temperature reactions in batch are well-established and diverse His work there focused on the development in the literature, the use of smaller reactor volumes in flow of new synthetic methods in the burgeoning reduces the risks associated with reactor failure and also field of photoredox catalysis. After obtaining facilitates reactor containment. The latter not only has safety his Ph.D. in 2015, Peter is now a implications, but also enables the insulation and recapturing of [3d] postdoctoral researcher in the lab of Tim lost energy more easily than in a larger batch process. Overall, Jamison. His current research focuses on from a manufacturing perspective, the opportunity to increase developing new methods to synthesize throughput and decrease residence time by accessing forcing bioactive molecules in flow. conditions (e.g. higher temperatures and pressures)[8] in an effective manner, has significant impacts for volume-time-output and the overall process efficiency.[9] Rachel Beingessner obtained her Ph.D. at the University of Ottawa in 2007 and then As an illustration of this concept, in 2010 we reported the batch joined the National Institute for and continuous flow synthesis of β-amino alcohols, a Nanotechnology – National Research functionality found in a number of active pharmaceutical Council Canada for one year of postdoctoral ingredients (APIs), which can be formed via the aminolysis of training prior to transitioning to a staff epoxide substrates.[10] As shown in Figures 2a and 2b, the ring research position. In 2015, she joined the opening of 2-(phenoxymethyl)oxirane (1) with tert-butylamine (2), Chemistry Department at MIT where she resulted in complete conversion and an 82% in situ yield of currently works as a Research Scientist. amine 3 under directly comparable flow and microwave batch conditions (150 °C for 30 min). However, by taking advantage of the ability to safely increase the reaction temperature from PERSONAL ACCOUNT 150 °C to 195 °C in flow, we were able to achieve an order of In addition to process intensification,[8] another significant magnitude reduction in the time scale of the reaction (3 min vs. attribute of a flow reactor is the high surface area to volume ratio 30 min), while maintaining a comparable yield and conversion that results from using small diameter tubing.
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