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298K时三元体系MeSO4-(NH42SO4-H2O的相平衡

Equilibrium Solubility in Ternary System of MeSO4-(NH42SO4-H2O at 298 K

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【作者】 慕思国彭长宏黄虹唐谟堂

【Author】 MU Si-guo, PENG Chang-hong, HUANG Hong, TANG Mo-tang (Inst. Environ. Eng., Sch. Metall. Sci. Eng., Central South University, Changsha, Hunan 410083, China)

【机构】 中南大学冶金科学与工程学院环境工程研究所中南大学冶金科学与工程学院环境工程研究所 湖南长沙410083湖南长沙410083

【摘要】 用等温溶解平衡法研究了298K时MeSO4?(NH4)2SO4?H2O三元体系的溶解度,并绘制了平衡相图.结果表明,在MnSO4?(NH4)2SO4?H2O体系中,有MnSO4?H2O,(NH4)2Mn(SO4)2?6H2O和(NH4)2SO43条饱和曲线,组成为MnSO4?H2O和(NH4)2Mn(SO4)2?6H2O及(NH4)2Mn(SO4)2?6H2O和(NH4)2SO4的2个共饱和点,以及平衡固相为(NH4)2SO4,(NH4)2Mn(SO4)2?6H2O和MnSO4?H2O的3个纯盐结晶区.在ZnSO4?(NH4)2SO4?H2O体系中,有(NH4)2Zn(SO4)2?6H2O,ZnSO4?7H2O与(NH4)2SO43条饱和曲线,组成为(NH4)2Zn(SO4)2?6H2O和ZnSO4?7H2O及(NH4)2SO4和(NH4)2Zn(SO4)2?6H2O的2个共饱和点,以及平衡固相为(NH4)2Zn(SO4)2?6H2O,ZnSO4?7H2O和(NH4)2SO4的3个纯盐结晶区.在(NH4)2SO4?FeSO4?H2O体系中,有(NH4)2Fe(SO4)2?6H2O,FeSO4?7H2O和(NH4)2SO4的3条饱和曲线,组成为(NH4)2Fe(SO4)2?6H2O和FeSO4?7H2O及(NH4)2Fe(SO4)2?6H2O和(NH4)2SO4的2个共饱和点,以及平衡固相为(NH4)2Fe(SO4)2?6H2O,FeSO4?7H2O和(NH4)2SO4的3个纯盐结晶区.研究结果既为含Fe2+,Mn2+和Zn2+溶液的复盐沉淀深度净化提供了理论指导,同时也为四元体系的研究奠定了基础.

【Abstract】 The phase equilibrium in the ternary system of MeSO4?(NH4)2SO4?H2O at 298 K was studied by isothermal equilibrium method and many significant experimental results were obtained. In the ternary system of MnSO4?(NH4)2SO4?H2O, there were 3 saturation curves given by MnSO4?H2O, (NH4)2Mn(SO4)2?6H2O and (NH4)2SO4, respectively. There were 2 co-saturation points, A having the composition of MnSO4?H2O and (NH4)2Mn(SO4)2?6H2O, and B given by (NH4)2Mn(SO4)2?6H2O and (NH4)2SO4. There were 3 purification crystallization areas given by (NH4)2Mn(SO4)2?6H2O, MnSO4?H2O and (NH4)2SO4, respectively. In the ternary system of ZnSO4?(NH4)2SO4?H2O, there were 3 saturation curves given by (NH4)2Zn(SO4)2?6H2O, ZnSO4?7H2O and (NH4)2SO4, respectively. There were 2 co-saturation points, C having the composition of (NH4)2Zn(SO4)2?6H2O and ZnSO4?7H2O, and D given by (NH4)2SO4 and (NH4)2Zn(SO4)2?6H2O, respectively. There were 3 purification crystallization areas given by (NH4)2Zn(SO4)2·6H2O, ZnSO4?7H2O and (NH4)2SO4, respectively. In the ternary system of FeSO4?(NH4)2SO4?H2O, there were 3 saturation curves given by (NH4)2Fe(SO4)2·6H2O, FeSO4?7H2O and (NH4)2SO4, respectively. There were 2 co-saturation points, E having the composition of (NH4)2Fe(SO4)2?6H2O and FeSO4?7H2O, and F given by (NH4)2Fe(SO4)2?6H2O and (NH4)2SO4, respectively. There were 3 purification crystallization areas of FeSO4?7H2O, (NH4)2Fe(SO4)2?6H2O and (NH4)2SO4, respectively. These experimental results gained above not only give theoretical guidance for the double-salt precipitation deep purification of such solutions containing Fe2+, Mn2+ and Zn2+, etc., but also establish foundation for study on the quarternary system consisting of Fe2+, Mn2+, Zn2+ and NH4+/SO42??H2O.

【关键词】 溶解度水盐体系相平衡
【Key words】 solubilitysalt?water systemphase equilibrium
【基金】 国家自然科学基金资助项目(编号:50444020);863计划资环领域资助项目(编号:2002AA649220)
  • 【文献出处】 过程工程学报 ,The Chinese Journal of Process Engineering , 编辑部邮箱 ,2006年01期
  • 【分类号】O642.42
  • 【被引频次】15
  • 【下载频次】246
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