Abstract
AbstractFor the cascade crystallization process a set of technological optimization conditions was established. The possibility of succesful application of proposed optimization conditions was pointed out by comparison with a mathematical model of Na2SO4 · 10 H2O crystallization in multichamber crystallizer presented in the literature. The method has a general applicability and can be used for the optimization of any cascade‐linked system, provided that the mathematical model was detailed enough to permit the operation of numerical derivation.
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