Zuofeng Yin, Yun Li, Hongfei Guo, Xiuwu Liu, Jilin Cao
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引用次数: 0
Abstract
To optimize the production process of K2SO4, this study employs the equilibrium cosaturated solution boiling evaporation crystallization method to determine the nonequilibrium-phase diagram of the Na+, K+//Cl–, SO42––H2O quaternary system under boiling evaporation conditions. Based on the nonequilibrium-phase diagram and the 25 °C equilibrium-phase diagram of the Na+, K+//Cl–, SO42––H2O system, the traditional two-step method for preparing and separating K2SO4 via the double decomposition reaction of KCl and Na2SO4 is optimized. Process calculations and experimental validations are conducted to evaluate the improvements. In addition to reducing the circulation volume of the mother liquor and the evaporation water volume, thereby lowering energy consumption, the optimized production process also achieved a 26.85% increase in the single-pass yield of the byproduct NaCl.
期刊介绍:
ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.