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Dynamic behaviour of an agitated two-phase reactor with dynamic variations in drop diameter-I

CHEMICAL ENGINEERING SCIENCE, no. 2 (1978): 205-217

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Abstract

A model assuming infinite drop coalescence and break-up rates was used to study the dynamic behaviour of chemically reacting liquid-liquid dispersions with simultaneous interphase heat and mass transfer in continuous reactors. The investigation has shown that, in some cases, it is important to take into account dynamic variations in inter...More

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