...
首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Solid-Liquid Equilibrium for the Ternary Systems (Na2SO4 + NaH2PO4 + H2O) and (Na2SO4 + NaCl + H2O) at 313.15 K and Atmospheric Pressure
【24h】

Solid-Liquid Equilibrium for the Ternary Systems (Na2SO4 + NaH2PO4 + H2O) and (Na2SO4 + NaCl + H2O) at 313.15 K and Atmospheric Pressure

机译:三元体系(Na2SO4 + NaH2PO4 + H2O)和(Na2SO4 + NaCl + H2O)在313.15 K和大气压下的固液平衡

获取原文
获取原文并翻译 | 示例

摘要

Solid-liquid equilibrium in the ternary systems (Na2SO4 + NaH2PO4 + H2O) and (Na2SO4 + NaCl + H2O) at 313.15 K and atmospheric pressure was investigated by using isothermal solution saturation and moist residue method. The solubility and thermodynamic properties of the solution were determined. The phase diagrams and the diagrams of thermodynamic properties versus composition were constructed. It turned out that there was one invariant point, two uninvariant curves, and two crystallization regions. In the phase diagram of the ternary system (Na2SO4 + NaH2PO4 + H2O) at 313.15 K, the crystallization region of Na2SO4 was obviously larger than the NaH2PO4 center dot 2H(2)O crystalline region. When Na2SO4 was 11.57 wt % and NaH2PO4 was 44.41 wt %, this system reached saturation at 313.15 K. In the phase diagram of the ternary system (Na2SO4 + NaCl + H2O) at 313.15 K, the crystallization region of Na2SO4 was significantly larger than the crystallization region of NaCl. When NaCl was 22.56 wt % and Na2SO4 was 5.00 wt %, this system reached saturation at 313.15 K. The research results could be used for the optimization solvent extraction process of sodium dihydrogen phosphate in industrial production.
机译:采用等温溶液饱和和湿残法研究了三元体系(Na2SO4 + NaH2PO4 + H2O)和(Na2SO4 + NaCl + H2O)在313.15 K和大气压下的固液平衡。测定溶液的溶解度和热力学性质。绘制了相图和热力学性质与组成的关系图。结果表明,存在一个不变点,两个不变曲线和两个结晶区域。在313.15 K的三元体系(Na2SO4 + NaH2PO4 + H2O)的相图中,Na2SO4的结晶区域明显大于NaH2PO4中心点2H(2)O的结晶区域。当Na2SO4为11.57 wt%,NaH2PO4为44.41 wt%时,该系统在313.15 K达到饱和。在三元体系(Na2SO4 + NaCl + H2O)的相图中,313.15 K,Na2SO4的结晶区明显大于NaCl的结晶区域。当NaCl为22.56 wt%,Na2SO4为5.00 wt%时,该体系在313.15 K下达到饱和。该研究结果可用于工业生产中磷酸二氢钠的溶剂萃取工艺优化。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号