Models are defined for various mixing conditions, in continuous flow systems. Differential equations are derived which take into account an effective volume of mixing, possible short‐circuiting, hold‐up time of the system, partial displacement or piston flow. The values of the different factors contained in the integrated equations can he determined experimentally by the particular response of a given system to a sudden change in composition of the feed. A correlation of the effective volume of mixing and the agitator r.p.m. is presented. A design procedure is suggested for tank flow reactors when partial mixing occurs.
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Cholette et al. (1959) studied this question.
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