In a flow reactor, the residence time (i.e. the amount of time that the reaction is heated or cooled) is calculated from the volume of the reactor and the flow rate through it.
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In this way, Syrris systems (such as Asia) are able to operate with reaction times from a few seconds to a few hours and can be used to synthesize mg to kg quantities in 24 hours.
In Syrris microreactors, reagents do not mix by turbulence (as in a batch reactor); instead, the reagents mix by diffusion. Because the distance across the chip reactor channel is approximately 200 μm, the time taken for reagents to completely diffuse is from a few milliseconds to a few seconds.
Syrris flow systems can be easily pressurized up to 20 bar. This allows reactions to be performed at temperatures much higher than atmospheric reflux, enabling faster and often cleaner, higher yielding reactions. Typically, solvents can be heated 60 to 150°C above their boiling point. Therefore reaction rate increases of the order of -fold are possible.
Examples of the superheating effect that can be achieved include:
The surface area to volume ratio of the reaction mixture in a Syrris reactor is s of times greater than a round bottom flask. Thus heat can be transferred to or from the reaction mixture much more rapidly than in a batch reactor. Greater temperature control can, therefore, be maintained for exo- or endothermic reactions improving consistency and yield.
Flow chemistry, continuous processing, or continuous flow chemistry, begins with two or more streams of different reactants pumped at specific flow rates into a single chamber, tube, or microreactor. A reaction takes place, and the stream containing the resultant compound is collected at the outlet. The solution may also be directed to subsequent flow reactor loops to generate the final product. Only small amounts of material are needed, which dramatically enhances process safety. Because of the inherent design of continuous flow technology, reaction conditions that cannot be safely achieved with batch reactions are possible. The result is product with higher quality, less impurity, and faster reaction cycle time.
Flow chemistry has been used for decades in the chemical industry. More recently, the pharmaceutical and fine chemical industries are increasingly adopting this technology. The inherent increased safety, improved product quality, cost efficiency, and overall production flexibility are drivers for the growing use of continuous flow chemistry.
Flow chemistry equipment generally consists of pumps that transport reactants, reagents, and solvent into reaction loops that introduce small volumes of reagents. These feed into a mixing junction where reagent streams are combined and passed into a coil reactor to provide reaction residence time. The reaction mixture may be fed into a column reactor that contains solid reagents, catalysts, or scavengers. An inline back pressure regulator controls the system, pressure and inline analytics are often used to provide information about reaction performance. Additionally, in situ FTIR spectroscopy can provide real-time feedback to proactively improve the reaction. For example, data from in situFTIR spectroscopy can be used to mitigate the effect of imperfect flow and control the addition rate of reagents for better mixing profile.
In recent years, the number and types of reactions that performed with continuous flow chemistry have grown substantially, especially in pharmaceuticals, fine chemicals, green chemistry, catalytic reactions, and polymer chemistry. Much of the growth is in chemistries that are too problematic to be handled on larger scale by batch reactions. These include potentially hazardous reactions such as:
Reactions for which reactants may be human health hazards are more safely handled by flow chemistry. Another growing use for continuous flow chemistry is to control stereochemistry, since reaction variables can be more carefully adjusted to control epimerization.
Flow chemistry is used for reactions where starting materials are in limited supply and small scale reactions are preferable.
When coupled with process analytical technology (PAT), flow chemistry allows for rapid analysis, optimization, and scale-up of a chemical reaction. With continuous real-time analysis, researchers monitor steady state conditions, troubleshoot process mishaps, and identify reactive intermediates. When flow chemistry is analyzed with Attenuated Total Reflectance (ATR), each functional group of a given substance has a unique fingerprint which can be trended over time and provides continuous measurement of component concentration as a function or process conditions. This provides a means to track the time and conditions necessary to reach and maintain steady state.
In this example, inline FTIR technology is used to analyze a continuous process that forms a thiomorpholine dioxide compound from the reaction of ethanolamine (EA) and divinylsulfone (DVS). Inline FTIR was used in both the development of the continuous process and in the monitoring of the chemistry carried out at larger scale. The scientists found that in small scale batch testing, this reaction was highly exothermic and potentially problematic if run at larger scale. Additionally, they pointed out that DVS is a toxic alkylating agent and exposure should be avoided.
To develop the continuous process, the reaction of EA with DVS was carried out in a 12 ml reactor, a ReactIR with flow cell was used to monitor the disappearance of DVS ( cm-1 band) and the appearance of the target compound ( cm-1 band). This reaction used water as a solvent, which did not interfere with the IR bands being tracked for DVS and compound 1. As the trace of these bands vs. time shows, once pump B was started, the cm-1 band from DVS appears. When pump A is actuated introducing EA, the DVS band disappears and the target compound appears and reaches steady state. The continuous flow reaction was adapted to larger equipment for kilogram scale production, and the ReactIR flow technology was employed to monitor the process in real-time.
Development of a Safe and High-Throughput Continuous Manufacturing Approach to 4‑(2-Hydroxyethyl)thiomorpholine 1,1-Dioxide Neil A. Strotman, Yichen Tan, Kyle W. Powers, Maxime Soumeillant, and Simon W. Leung, Bristol-Myers Squibb, New Brunswick, New Jersey , United States, Org. Process Res. Dev. , 22, 721−727
An FTIR spectrometer was introduced that is ideal for monitoring continuous flow chemistry in real time.
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The streamlined profile fits easily into physically constrained areas, meaning the instrument can be placed along the reaction sequence to monitor where needed.
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Infrared measurements can be made continually and unattended for as long as necessary to accommodate a synthesis.
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Set up and monitoring trends is straightforward and intuitive. Data from the ReactIR 702L can be integrated with control systems to allow for proactive execution of the chemistry.
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Mid-infrared analysis was to used to define the fraction conversion at each stage of the multiple fluidic module system, as well as the overall conversion and yield as a function of residence time. Key variables such as dosing rate, catalyst loading, and temperature were screened and optimized rapidly based on real-time information provided by heat flow calorimetry and in situ mid-infrared spectroscopy.
These tools also provided an understanding of which step controls the overall process rate as well as the effect that mixing and mass transfer and catalyst have on the reaction rate.
Performing reactions and processes in continuous flow mode can result in improved quality, safety and throughput. With Dynochem, the effect of important variables, including tube length, volume, temperature, residence time, can be readily modeled. Mixing effectiveness can be modeled in tubular and static mixing flow reactors. With respect to improved process safety for energetic reactions, Dynochem can aid in designing appropriate plug flow reactors based on heat flow data obtained from calorimetric measurements. Degree of conversion to product in Continuous Stirred Tank Reactor (CSTR) chains is easily modeled. Dynochem builds organizational confidence in the selection of the right type of reactor and reaction conditions for a process. Dynochem modeling is ideal for rapid optimization of conditions in flow reactors across product scales.
Below is a selection of recent continuous flow chemistry publications.
Wang Z., Gérardy R., Gauron, G., Damblon, C., Monbaliu, J-C., “Solvent-free organocatalytic preparation of cyclic organic carbonates under scalable continuous flow conditions”, React. Chem. Eng., , 4, 17-26
Harper, K., Moschetta, E., Bordawekar, S., Wittenberger, S., “A Laser Driven Flow Chemistry Platform for Scaling Photochemical Reactions with Visible Light”, ACS Cent. Sci. , 5, 109−115.
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Schulze, P., Leschinsky, M., Seidel-Morgenstern, A., Lorenz, H., “Continuous Separation of Lignin from Organosolv Pulping Liquors: Combined Lignin Particle Formation and Solvent Recovery”, Ind. Eng. Chem. Res. , 58, −
Wang, Z., Gérardy, R., Gauron, G., Damblon, C., Monbaliu, J-C., “Solvent-free organocatalytic preparation of cyclic organic carbonates under scalable continuous flow conditions”, React. Chem. Eng., , 4, 17-26
Dunn, A., Leitch, D., Journet, M., Martin, M., Tabet, E., Curtis, N., Williams, G., Goss, C., Shaw, T., O’Hare, B., Wade, C., Toczko, M., Li, P., “Selective Continuous Flow Iodination Guided by Direct Spectroscopic Observation of Equilibrating Aryl Lithium Regioisomers”, Organometallics, , 38 (1), pp 129–137
Musio, B., Gala, E., Ley, S., “Real-Time Spectroscopic Analysis Enabling Quantitative and Safe Consumption of Fluoroform during Nucleophilic Trifluoromethylation in Flow”, Sustainable Chem. Eng. , 6, −
Gérardy, R., Emmanuel, N., Toupy, TY., Kassin, V-E, Ntumba Tshibalonza, N., Schmitz, M., Monbaliu, J-C., “Continuous Flow Organic Chemistry: Successes and Pitfalls at the Interface with Current Societal Challenges”, Eur. J. Org. Chem. , –235.
Strotman, N., Tan, Y., Powers, K., Soumeillant, M., Leung, S., “Development of a Safe and High-Throughput Continuous Manufacturing Approach to 4‑(2-Hydroxyethyl)thiomorpholine 1,1-Dioxide”, Org. Process Res. Dev. , 22, 721−727.
Das, U., Higman, C., Gabidullin, B., Hein, J., Baker, R.T., “Efficient and Selective Iron-Complex-Catalyzed Hydroboration of Aldehydes”, ACS Catal. , 8, −.
Fitzpatrick, D., Ley, S., “Engineering chemistry for the future of chemical synthesis”, Tetrahedron, 74, 25, , Pages -
Galaverna, R., Breitkreitz, M., Pastre, J., “Conversion of D-Fructose to 5-(Hydroxymethyl)furfural: Evaluating Batch and Continuous Flow Conditions by Design of Experiments and In-Line FTIR Monitoring” ACS Sustainable Chem. Eng., , 6 (3), pp –
Yang, H., Martin, B., Schenkel B., “On-Demand Generation and Consumption of Diazomethane in Multistep Continuous Flow Systems”, Org. Process Res. Dev. , 22, 446−456.
Li, B., Guinness, S., Hoagland, S., Fichtner, M., Kim, H., Li, S., Maguire, R., McWilliams, J.C., Mustakis, J., Raggon, J., Campos, D., Voss, C., Sohodski, E., Feyock, B., Murnen, H., Gonzalez, M., Johnson, M., Lu, J., Feng, X., Sun, X., Zheng, S., Wu, B., “Continuous Production of Anhydrous tert-Butyl Hydroperoxide in Nonane Using Membrane Pervaporation and Its Application in Flow Oxidation of a γ‑Butyrolactam”, Org. Process Res. Dev. , 22, 707−720.
Pedersen, M., Skovby, T., Mealy, M., Dam-Johansen, K., Kiil, S., “Redesign of a Grignard-Based Active Pharmaceutical Ingredient (API) Batch Synthesis to a Flow Process for the Preparation of Melitracen HCl”, Org. Process Res. Dev. , 22, 228−235.
Hunter, S., Susanne, F., Whitten, R., Hartwig, T., Schilling, M., “Process design methodology for organometallic chemistry in continuous flow systems”, Tetrahedron, 74, 25, , -.
O’Brien, A., Ricci, E., Journet, M., “Dehydration of an Insoluble Urea Byproduct Enables the Condensation of DCC and Malonic Acid in Flow”, Org. Process Res. Dev., , 22 (3), pp 399–402
Fitzpatrick, D., Maujean, T., Evans, A., and Ley, S., “Across-the-World Automated Optimization and Continuous-Flow Synthesis of Pharmaceutical Agents Operating Through a Cloud-Based Server”, Angew. Chem. , 130,–
Hock, K., Koenigs, R., “The Generation of Diazo Compounds in Continuous‐Flow”, Chem. , 24(42), -.
Born S., Edwards, C., Martin, B., Jensen K., “Continuous, on-demand generation and separation of diphenylphosphoryl azide”, Tetrahedron., , 74(25), -
Ntumba Tshibalonza, N., Gérardy R., Alsafra, Z., Eppe, G., Monbaliu, J-C.,“A versatile biobased continuous flow strategy for the production of 3-butene-1,2-diol and vinyl ethylene carbonate from erythritol”, Green Chem., , 20, -
Thaisrivongs, D., Naber, J., Rogus, N., Spencer, G., “Development of an Organometallic Flow Chemistry Reaction at Pilot-Plant Scale for the Manufacture of Verubecestat”, Org. Process Res. Dev., , 22 (3), pp 403–408
Pedersen, M., Skovby T., Mealy, M., Kim Dam-Johansen, K., Kiil, S., “Redesign of a Grignard-Based Active Pharmaceutical Ingredient (API) Batch Synthesis to a Flow Process for the Preparation of Melitracen HCl”, Org. Process Res. Dev., , 22 (2), pp 228–235
Li, H., Sheeran, J., Clausen, A., Fang, Y-Q, Bio, M., Bader, S., “Flow Asymmetric Propargylation: Development of Continuous Processes for the Preparation of a Chiral b-Amino Alcohol”, Angew. Chem. Int. Ed. , 56, 1–6.
Ntumba Tshibalonza, N., Monbaliu, J-C., “Revisiting the deoxydehydration of glycerol towards allyl alcohol under continuous-flow conditions”, Green chemistry, , 13
Li, H., Sheeran, J., Clausen, A., Fang, Y-Q., Bio, M., Bader, S., “Flow Asymmetric Propargylation: Development of Continuous Processes for the Preparation of a Chiral β‐Amino Alcohol”, Angew. Chem. Int. Ed. , 56
Plutschack, M., Pieber, B., Gilmore, K., Seeberger, P., “The Hitchhiker’s Guide to Flow Chemistry”, Chem. Rev. , 117, −