CIESC Journal

• 化工学报 • 上一篇    

NH_3-H_3PO_4-H_2O体系汽液平衡的测定与热力学平衡计算

李仲英   

  1. 湖南大学环保研究所 长沙
  • 出版日期:1989-04-25 发布日期:1989-04-25

Thermodynamic Equilibria Calculation of NH_3-H_3PO_4-H_2O System

Li Zhongying (Hunan University,Changsha)   

  • Online:1989-04-25 Published:1989-04-25

摘要: 采用静态法测定了NH_3-H_3PO_4-H_2O体系在NH_3/H_3PO_4分子比为1.0-1.4,相应温度范围为75-175℃时的汽液平衡数据,并把实验数据关联成数学式.根据热力学理论,对NH_3-H_3PO_4-H_2O体系的热力学平衡计算的模型作了初步探讨.液相活度及活度系数采用扩充Pitzer方程,汽相逸度系数采用根据极性修改的RK方程.根据Edwards提出的弱电解质溶液的分子热力学,基于质量平衡、化学平衡、电荷平衡及汽液平衡理论,提出了NH_3-H_3PO_4-H_2O体系汽液平衡计算的热力学模型.计算结果表明:摩尔浓度低于25mol/kg H_2O时,模型计算结果与实验数据吻合得较好.

Abstract: A thermodynamic model of vapor-liquid equilibria in NH3-H3PO4-HO system has been studied. In the vapor liquid equilibria calculation by using extended Pitzer equation, water activity and solute activity coefficients in aqueous phase were obtained. By the modified Redlich-Kwong equation of state, vapor phase fugacity coefficients were obtained. Based on the assumption of Edwards et al (1975) of the molecular thermodynamics of aqueous weak electrolytes, a molecular thermodynamic correlation was established to calculate vapor liquid equilibria in NH3-H3PO4-H2O system. The correlation model calculated data agreed well with the experimental equilibrium vapor pressure data up to concentrations 25 mol/kgH2O.