672c Thermodynamics of Salt Lake System for Process Synthesis: Integration of Representation, Experiments and Visualization

Kui S. Kwok1, Maria E. Taboada2, Luis A. Cisternas2, and Ka M. Ng1. (1) Department of Chemical Engineering, Hong Kong University of Science and Technology, Clear Water Bay, Kowloon, Hong Kong, China, (2) Departamento de Ingenieria Quimica, Universidad de Antofagasta, Casilla 170, Antofagasta, Chile

Inorganic salts have wide applications in diverse fields. One of their major sources is salt lakes, and crystallization-based techniques have been utilized to extract the desired salts from the salt lake brine. For a feed with a given composition, the determination of which particular salt (or a mixture of salts) crystallizes under a specific set of operating conditions, and the development of the corresponding crystallization-based extraction process, requires knowledge of the solid-liquid equilibrium (SLE) phase behavior of the salt lake system and process design methods. Despite of the well establishment of phase-diagram based process synthesis procedures and process optimization methods, however, dealing with a salt lake system poses special challenges. The existence of a huge number of different species in a salt lake greatly complicates the representation, experimental determination and visualization of the thermodynamic data of such system, which thus causes difficulty in the process synthesis.

To tackle this problem, a coherent, systematic approach for the determination of solid-liquid phase behavior of a multi-component salt lake system for use in the synthesis of crystallization process is presented. It centers on the thermodynamics of such a salt lake system and integrates three interrelated activities - representation of the system phase behavior as a phase diagram/thermodynamic model, experimental determination of the necessary data and visualization of the relevant crystallization regions. To illustrate this approach, the thermodynamics of a simplified salt lake system Li+, Na+, K+, Mg2+//Cl-, SO42- - H2O at 25oC and 1 atm was determined. The identification of process alternatives using the resulting phase diagram for recovering Li2SO4*H2O was also demonstrated.