摘要
Solid-liquid equilibrium (SLE) values were experimentally determined for the NaCl-NH4 Cl-H2O system in the temperature range from 293.15 to 333.15 K, using the flow-cloud-point method (Zhang et al., 1998, Journal of Chemical and Engineering Data, 43, 32-37). A judicially selected equilibrium constant of NH4Cl, which is consistent with the available literature values, was used to determine a new Pitzer interaction parameter for pure NH4 Cl. This new parameter, together with the Pitzer mixing parameters determined from correlating the experimental values obtained in this work and some of the literature values, could be used to extend SLE for this system from 273.15 to 373.15 K, satisfying the process simulation requirement involved in the production of soda. (C) 2000 Elsevier Science Ltd. All rights reserved.
源语言 | 英语 |
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页(从-至) | 4993-5001 |
页数 | 9 |
期刊 | Chemical Engineering Science |
卷 | 55 |
期 | 21 |
DOI | |
出版状态 | 已出版 - 11月 2000 |