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Thermodynamics of aqueous electrolytes and hydrogen-bonded non-electrolytes over a wide range of temperature and pressure : the aqueous trivalent lanthanide cations and the methanol-water system

机译:水溶性电解质和氢键非电解质在很宽的温度和压力范围内的热力学:三价镧系元素阳离子和甲醇 - 水体系

摘要

Partial molar heat capacities and volumes of aqueous solutions are required to calculate the temperature- and pressure-dependence of chemical equilibrium constants over the wide range of conditions encountered in industrial and geochemical processes. Values for the standard partial molar heat capacities Cᴼp,₂ and volumes Vᴼ₂ of aqueous electrolytes also provide much information about the nature of the ionic solvation because both functions are sensitive to the hydrated structure of ions in solution. This research addresses two major topics. The objective of the first part of the program is to explore the solvation of M³⁺(aq) ions by determining the apparent molar volumes and heat capacities of several trivalent lanthanide ions over a wide range of temperature and pressure, and interpreting the results by semi-empirical hydration models. The second objective is to examine the behaviour of partial molar volumes in the methanol-water system, as an example of a hydrogen bonded non-electrolyte, over a range of temperature and pressure that approaches the critical locus of the mixture. -- Apparent molar heat capacities Cpφ and volumes Vφ were derived from specific heat capacities and densities measured in a Sodev Picker flow microcalorimeter and vibrating-tube densimeter at pressure 0.1 MPa. For high-temperature volumetric measurements, a stainless-steel cell vibrating tube densimeter and a platinum cell vibrating-tube densimeter were constructed in the course of this research. These densimeters allowed measurement of the densities of solutions relative to the reference fluid, water, at temperatures up to 600 K and pressures up to 30.0 MPa with an overall uncertainty less than 0.2 kg·m³. -- Data for Cpφ and Vφ for LaC1₃(aq), La(C1O₄)₃(aq), and Gd(C1O₄)₃(aq) from 283.2 K to 338.2 K; Nd(C1O₄)₃(aq), Eu(C1O₄)₃(aq), Er(C1O₄)₃(aq), and Yb(C1O₄)₃(aq) from 283.2 K to 328.2 K; and HCF₃SO₃(aq) and NaCF₃SO₃(aq) from 283.2 K to 328.2 K, were analysed by means of the Pitzer equations to derive Cᴼp,₂, Vᴼ₂, and expressions for the excess properties. The revised Helgeson-Kirkham-Flowers (HKF) model has been used to represent the temperature dependence of these standard partial molar properties within the experimental uncertainty. Plots of Cᴼp,₂ and Vᴼ₂, at T = 298.15 K against the ionic radius of the six lanthanide cations clearly display the discontinuous behaviour known as the "gadolinium break". It was found that the ionic-radius dependence of Vᴼ₂ is consistent with changes in the primary hydration number, while the effect of temperature on the behaviour of Cᴼp,₂ across the series suggests that secondary sphere hydration has a major effect on C° 2. -- Densities of NaCF₃SO₃(aq) and Gd(CF₃SO₃)₃(aq) were measured with the platinum-cell vibrating tube densimeter at temperatures from 323 K to 600 K and at pressures up to 20 MPa. Apparent molar volumes for NaCF₃SO₃(aq) and Gd(CF₃SO₃)₃(aq) calculated from the measured densities were represented by the Pitzer ion-interaction treatment. The temperature and pressure dependence of Vᴼ₂ and the second viriai coefficients in the Pitzer equation were expressed by empirical expressions in which the compressibility of water was used as an independent variable. These treatments led to values of Vᴼ₂(NaCF₃SO₃, aq) from 283 K to 573 K and Vᴼ₂Gd(CF₃SO₃)₃, aq) from 278 K to 473 K as functions of temperature and pressure, which are the first reported in the literature. The conventional values of Vᴼ₂(Gd³⁺, aq) calculated from these data and Vᴼ₂(Na⁺, aq) from the literature are in excellent agreement with extrapolations of low-temperature values of Vᴼ₂(Gd(C1O₄)₃, aq) based on the HKF approach. It was found that the effect of pressure on Vᴼ₂ for Gd(CF₃SO₃)₃(aq) was more pronounced than that for common 1:1 and 2:1 aqueous electrolytes at temperatures near 298 K, and that this behaviour could be explained by the larger primary hydration shell for trivalent lanthanide cations. -- Densities of {xCH₃OH + (1 - x)H₂O} relative to water were measured in the vibrating tube densimeter at the temperatures T = (323, 373, 423, 473, 523, and 573 K) and at pressures of 7.0 MPa and 13.5 MPa. Excess molar volumes VᴱM for {xCH₃OH + (1 - x) H₂O} were calculated from the experimental densities for the mixtures, using accurate equations of state for water and methanol. The data were treated with an extended corresponding-states model based on the properties of pure water. An empirical function was used to fit small differences between the compression factors of {xCH₃OH + (1 - x) H₂O} and the compression factor of H₂O at the same reduced temperature and the same reduced pressure. The corresponding-states treatment reproduces the measured densities to within the experimental uncertainty of 0.0004 g-cm⁻³ at all of the temperatures and pressures studied, except at T = 573 K and p = 13.5 MPa. The densities, excess molar volumes, partial molar volumes, isothermal compressions, and cubic expansion coefficients from the model are consistent with the limited literature data available. The behaviour of VᴱM at T = 573.6 K, and p = 13.7 MPa indicates either a very narrow region of (vapour + liquid) phase separation, or near-critical behaviour at x = 0.44 with the critical pressure pc ≤ 13.5 MPa.
机译:在工业和地球化学过程中遇到的各种条件下,需要部分摩尔热容和水溶液的体积来计算化学平衡常数的温度和压力依赖性。含水电解质的标准部分摩尔热容C₂p,2和体积Vᴼ2的值也提供了有关离子溶剂化性质的许多信息,因为这两种功能都对溶液中离子的水合结构敏感。这项研究涉及两个主要主题。该程序第一部分的目的是通过确定几种三价镧系离子在很宽的温度和压力范围内的表观摩尔体积和热容量,并通过半解析来解释M³(aq)离子的溶剂化作用。 -经验水化模型。第二个目的是在接近混合物临界点的温度和压力范围内,检查甲醇-水系统中部分摩尔体积的行为,作为氢键合非电解质的一个例子。 -表观摩尔热容Cpφ和体积Vφ由在0.1 MPa压力下的Sodev Picker流动微热量计和振动管密度计中测得的比热容和密度得出。为了进行高温体积测量,在研究过程中构建了不锈钢电池振动管密度计和铂电池振动管密度计。这些密度计可以在温度高达600 K,压力高达30.0 MPa的条件下测量相对于参考流体,水的溶液密度,总不确定度小于0.2 kg·m³。 -LaC1₃(aq),La(C1O₄)₃(aq)和Gd(C1O₄)₃(aq)的Cpφ和Vφ数据从283.2 K到338.2 K; Nd(ClO 3)3(aq),Eu(ClO 3)3(aq),Er(ClO 3)3(aq)和Yb(ClO 3)3(aq)从283.2K到328.2K;用Pitzer方程分析了从283.2K到328.2K的HCF 3 SO 3和NaCF 3 SO 4(aq)和NaCF 3 SO 4(aq),得到C 1 p,2,V 12和过量性质的表达式。修改后的Helgeson-Kirkham-Flowers(HKF)模型已用于表示实验不确定性范围内这些标准部分摩尔特性的温度依赖性。在T = 298.15K处,相对于六个镧系元素阳离子的离子半径的Cᴼp,2和Vᴼ2曲线清楚地显示出不连续的行为,称为“ ga断裂”。发现Vᴼ2的离子半径依赖性与一次水合数的变化是一致的,而温度对整个系列中Cᴼp,2行为的影响表明,二次球面水合对C°2具有重要影响。 -用铂电池振动管密度计在323 K至600 K的温度和最高20 MPa的压力下测量NaCF 3 SO 3(aq)和Gd(CF 3 SO 4)3(aq)的密度。由Pitzer离子相互作用处理表示由测得的密度计算出的NaCF 3 SO 3(aq)和Gd(CF 3 SO 4)3(aq)的表观摩尔体积。通过将水的可压缩性用作自变量的经验表达式来表达Pitzer方程中的Vᴼ2的温度和压力依赖性以及第二维里亚系数。这些处理导致了温度和压力的函数,V 2(NaCF 3 SO 4,aq)从283K到573 K和V 12 Gd(CF 3 SO 4,aq)从278 K到473 K作为温度和压力的函数,这是在文献中首次报道的。根据这些数据计算出的常规的V 12(Gd 3+,aq)值和根据文献得出的V 12(Na 3,aq)与根据V 2(Gd(ClO 3)3,aq)的低温值的外推法非常一致。 HKF方法。已发现,在298 K附近,Gd(CF 3 SO 4)3(aq)的压力对Vᴼ2的影响比普通的1:1和2:1水性电解质的影响更为明显,这种现象可以用三价镧系元素阳离子的较大一级水合壳。 -在温度T =(323、373、423、473、523和573 K)和压力为7.0 MPa的条件下,在振动管密度计中测量{xCH = OH +(1-x)H 2 O}相对于水的密度和13.5 MPa。 {xCH = OH +(1-x)H 2 O}的过量摩尔体积VᴱM是使用精确的水和甲醇状态方程,根据混合物的实验密度计算得出的。根据纯水的性质,使用扩展的对应状态模型处理数据。使用经验函数来拟合{xCH = OH +(1-x)H 2 O}的压缩因子与H 2 O的压缩因子在相同的降低温度和相同的降低压力之间的微小差异。在所有研究的温度和压力下,除了在T = 573 K和p = 13.5 MPa时,相应状态的处理都将所测得的密度再现到0.0004 g-cm 3的实验不确定度之内。密度,过量摩尔体积,部分摩尔体积,等温压缩和模型的三次膨胀系数与可用的有限文献数据一致。 VᴱM在T = 573.6 K和p = 13.7 MPa时的行为表明(蒸气+液相)相分离的区域非常狭窄,或者在x = 0.44且临界压力pc≤13.5 MPa时接近临界行为。

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    Xiao Caibin;

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  • 年度 1997
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  • 原文格式 PDF
  • 正文语种 {"code":"en","name":"English","id":9}
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