Comprehensive Organic Synthesis II 2014
DOI: 10.1016/b978-0-08-097742-3.00912-5
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9.03 Organic Synthesis in Small Scale Continuous Flow: Flow Chemistry

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Cited by 4 publications
(2 citation statements)
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“…the specific reaction rate, r) of a continuous-flow reaction (r f ) and of the corresponding one in batch mode (r b ) were compared at similar degrees of conversions (> 49 %). As shown in Table 3, in KRs of amines 1.5-2 higher r flow values could be achieved in packed-bed microreactors as compared to the r batch values in batch system (in accordance with the known benefit of continuous-flow systems compared to batch reactors [82]).…”
Section: Kinetic Resolution Of Racemic Amines Rac-3a-e With M540-f-calbsupporting
confidence: 70%
“…the specific reaction rate, r) of a continuous-flow reaction (r f ) and of the corresponding one in batch mode (r b ) were compared at similar degrees of conversions (> 49 %). As shown in Table 3, in KRs of amines 1.5-2 higher r flow values could be achieved in packed-bed microreactors as compared to the r batch values in batch system (in accordance with the known benefit of continuous-flow systems compared to batch reactors [82]).…”
Section: Kinetic Resolution Of Racemic Amines Rac-3a-e With M540-f-calbsupporting
confidence: 70%
“…Application of microreactors is associated with process intensification meaning a reduction in equipment size by several orders of magnitude, thus causing a remarkable decrease in capital and energy costs and a positive environmental impact [1][2][3]. The commonly known advantages of microscale reactor technology are related to a high surface-area-to-volume ratio (because of thin channels), enhanced heat and mass transfer [4][5][6] and straightforward scale-up, because conventional scale-up is replaced by number-up [7]: a sufficient production volume is obtained by coupling microscale units in parallel.…”
Section: Introductionmentioning
confidence: 99%