首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Thermodynamically Traceable Calorimetric Results for Dilute Aqueous Potassium Chloride Solutions at Temperatures from (273.15 to 373.15) K. Part 1. The Quantities Associated with the Partial Molar Enthalpy
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Thermodynamically Traceable Calorimetric Results for Dilute Aqueous Potassium Chloride Solutions at Temperatures from (273.15 to 373.15) K. Part 1. The Quantities Associated with the Partial Molar Enthalpy

机译:热力可追踪的热量热量,用于在(273.15至373.15)K的温度下稀释氯化钾水溶液的热量测量结果。第1部分。与部分磨牙焓相关的数量

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In our previous study (Partanen, J. I.; Partanen, L. J.; Vahteristo, K. P., J. Chem. Eng. Data 2019, 64, 16-33), we presented a fully traceable two -parameter Huckel equation with parameters B and b(1) for activity and osmotic coefficients in dilute KCl(aq) in the temperature range of (273.15 to 383.15) K. This equation applies within experimental error to almost all thermodynamic data in the literature at least up to a molality of 0.2 mol.kg(-1). In our Hiickel model, parameter B is treated as a constant, whereas parameter b(1) depends quadratically on the temperature. In the present study, the same model is applied to the molar enthalpies of the components in KCl solutions. No new parameter estimations are necessary for the treatment of these calorimetric data. We also extend now the previous enthalpy results for dilute NaCl solutions (see Partanen, J. I.; Partanen, L. J.; Vahteristo, K. P., J. Chem. Eng. Data 2017, 62, 2717-2632) up to 373 K because in that study the treatment of calorimetric data was limited only up to 353 K. In a future publication (Part 2 of this study), it will be shown that this Hiickel model applies additionally well to the heat-capacity literature available for dilute KCl solutions. Here, we also consider a second parametrization of the Hiickel equation for KCl solutions obtained in a previous work (Partanen, J. I., J. Chem. Eng. Data 2016, 59, 286-306). This is seen to apply better to enthalpy data in less dilute KCl solutions up to the saturated solutions in the range of (298 to 303) K. However, the alternative parametrization is not fully traceable and not as accurate as our primary one. Following the success of these Hiickel models, we supplement the thermodynamic tables for KCl solutions with the relative apparent and partial molar enthalpies of KCl in these solutions from (273.15 to 373.15) K. We also give here the values of these quantities for NaCl in dilute aqueous NaCl solutions at 373.15 K. We have good reason to believe that the new tables contain the most reliable values available for the enthalpy quantities of dilute NaCl and KCl solutions.
机译:在我们以前的一项研究中(吉; LJ; Vahteristo,KP,J.Chem。Eng。ENG。ENG。数据2019,64,16-33),我们呈现了一个完全可追踪的两个-Parameter Huckel方程,具有参数B和B(1 )在(273.15至383.15)的温度范围内的稀释kcl(aq)中的活性和渗透系数。该方程在实验误差内应用于文献中的几乎所有热力学数据,至少达到0.2 mol.kg的麦格力( -1)。在我们的HIICKEL模型中,参数B被视为常数,而参数B(1)则在二次上取决于温度。在本研究中,相同的模型应用于KCl溶液中组分的摩尔焓。对于处理这些量热数据,不需要新的参数估计。我们现在还延长了以前的稀释NaCl解决方案的焓结果(参见Partanen,Ji; Partanen,LJ; Vahteristo,KP,J.Chem。Eng。数据2017,62,2717-2632)高达373 k,因为在那里研究热量数据的处理仅限于高达353 K.在未来的出版物(本研究的第2部分)中,将表明,这种Hiickel模型适用于可用于稀释KCl溶液的热容量。这里,我们还考虑在先前的工作中获得的KCl溶液的Hiickel方程的第二位参数化(Partanen,J.I,J.Chem。ENG。数据2016,59,286-306)。这被认为,在较少的稀释KCl溶液中升高到(298至303)K的范围内的饱和溶液中的焓数据更好地应用。然而,替代的参数化并不完全可追溯,而不是如我们的主要溶液。在这些Hiickel模型的成功之后,我们将KCl解决方案的热力学表与KCl的相对明显和部分摩尔焓从(273.15至373.15)K中进行了相对明显的和部分摩尔焓。我们还提供了稀释的NaCl的这些量的值NaCl水溶液在373.15 K.我们有充分的理由相信,新表含有最可靠的值可用于稀释NaCl和KCl溶液的焓。

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