Abstract
AbstractThis paper presents a novel theoretical approach for maximizing productivity in microreactors by a controlled extension of the tube diameter. A one-dimensional numeric model was developed where the tube diameter increases based on the reaction heat to achieve a constant temperature throughout the reactor length. Through this approach, a basic plug flow reactor model for mass and heat transfer was used with an integrated algorithm for a controlled diameter extension. A parametric study was performed to ensure safe operating conditions concerning thermal runaway. The results show an increase in productivity of approximately 42% for the fictional second-order test reaction.
Graphical abstract
Publisher
Springer Science and Business Media LLC
Subject
Organic Chemistry,Fluid Flow and Transfer Processes,Chemistry (miscellaneous)
Cited by
2 articles.
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