A network flow model is presented for synthesizing crystallization-based separations for multicomponent systems. The construction of the network flow is based on the identification of feasible thermodynamic states. The method allows consideration of se®eral operation temperatures, complex solid ᎐ li
Design of separation schemes for fractional crystallization of metathetical salts
✍ Scribed by Luis A. Cisternas; Mauricio A. Torres; María J. Godoy; Ross E. Swaney
- Publisher
- American Institute of Chemical Engineers
- Year
- 2003
- Tongue
- English
- Weight
- 380 KB
- Volume
- 49
- Category
- Article
- ISSN
- 0001-1541
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✦ Synopsis
Abstract
The synthesis method of fractional crystallization processes for the separation of salts belonging to reciprocal salt pairs is presented based on a flow network model constructed between thermodynamic states. The state nodes represented in the model include feeds, products, intermediate products, and solid–liquid equilibrium states. Flows between the states are represented by arcs within the flow model. A systematic procedure is given for identification of the solid–liquid equilibrium states that could potentially serve as operating points. This identification is essential to the construction of the flow network and reduces the problem to a simple mathematical form. The advantages of the method lie in its capability to consider general process flow pattern, handle systems forming double salt, deal with several temperatures as potential operation conditions, and handle several feeds and products. Examples are given to illustrate the procedure.
📜 SIMILAR VOLUMES
In conventional metathetical reactions, product separation is based on solubility product differences, and the resulting products are often impure and require purification by recrystallization. A new approach to product separation is described that relies on the formation of an unstable, volatile by