Applicability of the axial dispersion model to coiled flow inverters containing single liquid phase and segmented liquid-liquid flows

Continuous diameter increase reactor – a reactor concept for maximizing productivity by a controlled diameter extension

This 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

Characterization of axial dispersion in vertical helical coil for gas-liquid-liquid flow at low Reynolds numbers

Gas-Liquid-Liquid (GLL) slug flow reactors offer several advantages like higher interfacial area, excellent mass transfer, and lower backmixing. The mesoscale (diameter ~ few mm) helical coiled reactors operating in slug...