首页> 外文期刊>Journal of Solution Chemistry >Thermodynamic modeling of aqueous aluminum chemistry and solid-liquid equilibria to high solution concentration and temperature. I. The acidic H-Al-Na-K-Cl-H2O system from 0 to 100 degrees C
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Thermodynamic modeling of aqueous aluminum chemistry and solid-liquid equilibria to high solution concentration and temperature. I. The acidic H-Al-Na-K-Cl-H2O system from 0 to 100 degrees C

机译:铝水化学和固液平衡至高溶液浓度和温度的热力学模型。 I.酸性H-Al-Na-K-Cl-H2O系统从0到100摄氏度

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In this paper, we describe the development of a thermodynamic model that calculates solute/solvent activities and solid-liquid equilibria in the acidic aluminum system, H-Al3+-Na-K-Cl-H2O, to high molality from 0 degrees to approximate to 100 degrees C. The model incorporates the concentration-dependent, specific interaction equations for aqueous solutions of Pitzer (Activity Coefficients in Electrolyte Solutions, 2nd edn., pp. 75-153, CRC Press, Boca Raton, 1991). Parameterization of this model adds Al3+ specific interactions in the binary Al-Cl-H2O and ternary Al-H-Cl-H2O, Al-Na-Cl-H2O and Al-K-Cl-H2O systems as well as the standard chemical potentials of AlCl3 center dot 6H(2)O(s) and Al(OH)(3)(s) (gibbsite) in the 0 degrees to 100 degrees C range to our variable temperature (0-250 degrees C) model of acid-base reactions in the H-Na-K-OH-Cl-HSO4-SO4-H2O system (Christov and Moller in Geochim. Cosmochim. Acta 68:1309, 2004). In constructing our aluminum model, we used Emf, osmotic, equilibrium constant and solubility data. New Emf measurements using the cell Pt broken vertical bar H-2(g, 101.325 kPa)broken vertical bar HCl(m (1)), AlCl3(m (2))broken vertical bar AgCl(s)broken vertical bar Ag broken vertical bar Pt at temperatures ranging from 0 to 45 degrees C and at total ionic strength ranging from 0.1 to 3 mol kg(-1) are presented. Gibbsite and boehmite, AlOOH(s), solubility data are used in testing the model. Limitations of the model due to data insufficiencies are discussed.
机译:在本文中,我们描述了一种热力学模型的开发,该模型可计算酸性铝系统H-Al3 + -Na-K-Cl-H2O中溶质/溶剂活性和固液平衡,从0度到大约100摄氏度。该模型结合了Pitzer水溶液的浓度依赖性特定相互作用方程式(电解质溶液中的活度系数,第二版,第75-153页,CRC出版社,Boca Raton,1991)。该模型的参数化在二元Al-Cl-H2O和三元Al-H-Cl-H2O,Al-Na-Cl-H2O和Al-K-Cl-H2O系统中添加了Al3 +特定的相互作用以及在0到100摄氏度范围内的AlCl3中心点6H(2)O(s)和Al(OH)(3)(三水铝石)到我们的酸碱可变温度(0-250摄氏度)模型H-Na-K-OH-Cl-HSO4-SO4-H2O系统中的反应(Christov和Moller in Geochim。Cosmochim。Acta 68:1309,2004)。在构建铝模型时,我们使用了电动势,渗透压,平衡常数和溶解度数据。使用电池Pt的新Emf测量垂直断线H-2(g,101.325 kPa)垂直断线HCl(m(1)),AlCl3(m(2))垂直断线AgCl(s)垂直断线Ag垂直断线给出了在0到45摄氏度的温度范围和0.1到3 mol kg(-1)的总离子强度范围内的bar Pt。锡矿和勃姆石AlOOH的溶解度数据用于测试模型。讨论了由于数据不足而导致模型的局限性。

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