An Integrated Microreactor System for Self-Optimization of a Heck Reaction: From Micro- to Mesoscale Flow Systems
An Integrated Microreactor System for Self-Optimization of a Heck Reaction: From Micro- to Mesoscale Flow Systems
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DOI:
10.1002/anie.201002590
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发表时间:
2010-01-01
影响因子:
16.6
通讯作者:
Jensen, Klavs F.
中科院分区:
文献类型:
--
作者:
McMullen, Jonathan P.;Stone, Matthew T.;Jensen, Klavs F.
Continuous flow processes offer several advantages over traditional batch synthesis including ease of scale up [1, 2] and the ability to run reactions safely at extreme pressures and temperatures.[3–6] Microreactors in particular have been shown to have superior heat and mass transfer rates,[7–9] providing precise control of reaction conditions.[10] These attributes make microreactors ideal for fast reactions,[11] highly exothermic reactions,[12] explosive reactions,[13] and reactions that involve energetic intermediates.[14] The small volume capacity of microreactors has also allowed the efficient development of more sophisticated continuous flow reactions on increasingly complex molecular targets since they greatly reduce the quantities of materials needed to optimize reaction conditions.[8, 15–20] However, the specialized equipment required for microreactor flow systems also increases the difficulty of screening reaction conditions in parallel as is commonly performed in batch. Thus, developing efficient strategies to optimize reaction conditions in a series of consecutive experiments is particularly valuable for microreactors. Towards this end we have developed a self-optimizing microreactor system that uses previous reaction data to efficiently select future experiments. This approach allows numerous parameters to be optimized simultaneously. Several automated microreactors systems have been developed that are capable of sampling a series of predetermined reaction conditions. These systems often employ a univariable approach in which only a single variable is adjusted at a time.[21] Such exhaustive searches are inherently inefficient since they are likely to gather a significant percentage of data points that are far away from the desired maximum. A more sophisticated automated microreactor system based on Design of Experiment methods has also been developed. Although this system is ideally suited for response surface modeling, the approach is less efficient in terms of the number of reactions required for an optimization.[22] Integrating feedback into the reaction optimization could significantly increase the speed and efficiency of the overall process by directing the system away from lower yielding reaction conditions.[23] Furthermore, reaction optimization results obtained in a microreactor are typically not limited by mass or heat transfer effects. Consequently, moving from optimal laboratory conditions to larger scale reactors can be more easily achieved by integrating the observed chemical understanding with established chemical engineering reactor design methods.[24–26]Herein we describe a self-optimizing microreactor system that employs a “black-box” optimization technique directed by the Nelder–Mead Simplex Method.[27] The system was shown to maximize the yield of a Heck reaction by adjusting the equivalents of the alkene and the residence time. Upon obtaining optimized conditions in a microreactor, the reaction was scaled-up 50-fold in a mesoscale flow reactor. Reaction conditions were surveyed in the mesoscale reactor and found to be in good agreement with the yields observed in the microreactor. The optimal residence time and equivalents of alkene were then allowed to run in the mesoscale reactor for 22 reactor volumes (ca. 2h) and upon purification the resulting isolated yield was found to be in good agreement with the online HPLC analysis. We chose to examine the Heck reaction of 4-chlorobenzotrifluoride (1) and 2, 3-dihydrofuran (2; Scheme 1) since the desired product 3 readily reacts with a second equivalent of the aryl chloride.[28] Thus, the yield of the reaction is highly dependent upon the number of …