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Thermodynamics and Solubility Modeling in Hydrofluoroalkane Systems

机译:氢氟烷烃体系中的热力学和溶解度建模

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摘要

The phase-out of chlorofluorocarbons (CFCs) has resulted in an expanding new area of research in alternative ozone friendly propellants, for example hydrofluoroalkanes (HFAs). The HFA solvent system is unique in that many CFC soluble compounds behave differently in the HFA alternatives, such as HFA-134a and HFA-227. The reason for the difference in solubility is not fully recognized. This work investigates the solubility of 22 compounds in HFA-227 with the addition of ethanol as a cosolvent. The physical properties of both solute and solvent were investigated in order to determine the effects on solubility. The solubilities of 5 compounds in HFA-134a were also investigated. A thermodynamic approach was utilized in order to look at the enthalpic and entropic effects on solubility in the propellant. Due to the high vapor pressure of propellants, a liquid model was utilized, owing to its ease of use in characterizing solubility. The correlation between the liquid model 2H,3H-decafluoropentane (DFP) and the propellants HFA-134a and HFA-227 was examined.The solubilities in HFA-227 with ethanol ranged from 0.001 to 3.282 %w/w, where the solubilities always increase when ethanol was added. The experimental solubilities were compared to calculated values obtained from ideal solubility and regular solution theory models. A clear correlation with the ideal solubility (melting point) combined with an intercept term and two physical properties was noted. A regression approach was also used to predict the activity coefficient in HFA-227 with 0 - 20% ethanol. These equations were combined with the extended ideal solubility equation, creating a useful predictive equation with AAE values ranging from 0.32 to 0.36, or factor errors of 2.09 to 2.29. The equations shown in this work are useful for the prediction of solute solubility in HFA-227/ethanol mixtures.Results in the liquid model DFP with 0 - 20% ethanol show that a regression equation results in a useful predictive equation for the solubilities in both HFA-134/ethanol and HFA-227/ethanol systems, where the AAE values ranged from 0.3 to 0.56, or factor errors of 2.0 to 3.6.The solubilities of a series of chlorobenzene compounds along with a group of hydrogen donating and/or accepting compounds was examined in HFA-134a. The entropic effects appear to be the limiting factor in the solubility of these compounds. The compounds capable of hydrogen accepting and donating exhibited negative enthalpy of mixing values when placed in HFA-134a, a stark contrast to the values obtained for the chlorobenzenes. This suggests HFA-134a is able to strongly interact with solutes capable of donating or accepting hydrogen.
机译:逐步淘汰含氯氟烃(CFC)导致了替代臭氧友好推进剂(例如氢氟烷烃(HFA))研究的新领域不断扩大。 HFA溶剂系统的独特之处在于,许多可溶于CFC的化合物在HFA替代品(例如HFA-134a和HFA-227)中表现不同。溶解度差异的原因尚未完全认识。这项工作研究了22种化合物在HFA-227中的溶解度,并添加了乙醇作为助溶剂。研究了溶质和溶剂的物理性质,以确定对溶解度的影响。还研究了5种化合物在HFA-134a中的溶解度。为了观察焓和熵对推进剂溶解度的影响,采用了热力学方法。由于推进剂的高蒸气压,使用了液体模型,因为它易于表征溶解度。研究了液体模型2H,3H-十氟戊烷(DFP)与推进剂HFA-134a和HFA-227之间的相关性.HFA-227在乙醇中的溶解度范围为0.001至3.282%w / w,其中溶解度始终在增加当添加乙醇时。将实验溶解度与从理想溶解度和常规溶液理论模型获得的计算值进行比较。注意到与理想的溶解度(熔点)结合一个截距项和两个物理性质有着明显的相关性。还使用回归方法来预测0-20%乙醇在HFA-227中的活度系数。这些方程式与扩展的理想溶解度方程式组合,创建了一个有用的预测方程式,其AAE值在0.32至0.36或因子误差为2.09至2.29的范围内。这项工作中显示的方程式对于预测HFA-227 /乙醇混合物中的溶质溶解度非常有用。在DFP模型中,乙醇含量为0-20%的液体模型的结果表明,回归方程式可以得出两种溶解度的有用预测方程式HFA-134 /乙醇和HFA-227 /乙醇系统,其AAE值介于0.3至0.56之间,或因子误差介于2.0至3.6之间。一系列氯苯化合物的溶解度以及一组供氢和/或接受氢的化合物在HFA-134a中检查了这些化合物。熵效应似乎是这些化合物溶解度的限制因素。当置于HFA-134a中时,能够接受和给予氢的化合物显示出负的混合焓值,这与氯苯的值形成了鲜明的对比。这表明HFA-134a能够与能够提供或接受氢的溶质强烈相互作用。

著录项

  • 作者

    Hoye William L;

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  • 年度 2008
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  • 原文格式 PDF
  • 正文语种 EN
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