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SOLUBILITY STUDIES IN PURE AND MIXED SOLVENTS (PYRIDINE, THIOPHENE, BENZENE, CYCLOHEXANE).

机译:纯和混合溶剂(吡啶,噻吩,苯,环己烷)中的溶解度研究。

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摘要

The research presented in this dissertation consists of two parts; part 1 for solubility of aromatic hydrocarbon solids in pure and mixed solvents and part 2 for solubility of pure gases in water at high pressures.;In the research of part 2, equilibrium compositions of vapor and liquid phases for binary systems CH(,4)-H(,2)O and N(,2)-H(,2)O are measured at pressures of up to 101.3 MPa at 323 and 373K. The solubility data are correlated by the modified Krichevsky-Kasarnovsky equation. The Krichevsky-Ilinskaya equation, on the other hand, is proved inadequate for the correlation of the gas solubility data of this research. Instead, an equation which includes a term for the coefficient of isothermal compressibility of the partial molar volume in addition to a non-ideality term correlates the solubility data well. Solubilities of the gases in water at high pressures are predicted by the modified Krichevsky-Kasarnovsky equation using the apparent partial molar volume estimated by the method suggested in this study.;In the research of part 1, eight aromatic hydrocarbon solids biphenyl, naphthalene, fluorene, phenanthrene, acenaphthene, fluoranthene, pyrene and o-terphenyl are employed to measure their solubilities in pure solvents pyridine and thiophene and in mixed solvents of benzene and cyclohexane at three different concentrations. Solubilities of phenanthrene, which undergoes a lambda point transition, are predicted by a new solubility equation derived in this research. The new equation includes a term for the contribution of the phase transition. Activity coefficients of solids are predicted by the Scatchard-Hildebrand regular solution equation by using the solubility parameters evaluated by the floating datum point method, which is devised in this study. Solubilities of the solids are generalized for each of the solvents as suggested by McLaughlin and Zainal.
机译:本文的研究分为两个部分。第1部分是芳香烃固体在纯净和混合溶剂中的溶解度,第2部分是纯净气体在高压下在水中的溶解度。;在第2部分的研究中,二元系统CH(,4)的气相和液相平衡组成-H(,2)O和N(,2)-H(,2)O是在323和373K压力高达101.3 MPa的条件下测量的。溶解度数据通过修改后的Krichevsky-Kasarnovsky方程进行关联。另一方面,事实证明Krichevsky-Ilinskaya方程不足以证明该研究的气体溶解度数据具有相关性。取而代之的是,除了非理想项之外,还包括部分摩尔体积的等温压缩系数的项的方程式与溶解度数据很好地相关。通过修改后的Krichevsky-Kasarnovsky方程,使用本研究建议的方法估算的表观部分摩尔体积,可预测高压下气体的溶解度。在第1部分的研究中,八个芳香烃固体联苯,萘,芴用菲,,荧蒽,pyr和邻三联苯测量在纯溶剂吡啶和噻吩以及在苯和环己烷的混合溶剂中的三种不同浓度下的溶解度。通过这项研究得出的新溶解度方程可以预测菲的溶解度,该菲经历了λ点跃迁。新的方程式包括相变贡献项。固体的活度系数由Scatchard-Hildebrand正则方程通过使用浮点基准法评估的溶解度参数来预测,这是本研究设计的。如McLaughlin和Zainal所建议,对每种溶剂都可以概括固体的溶解度。

著录项

  • 作者

    CHOI, PETER BYONGHYOCK.;

  • 作者单位

    Louisiana State University and Agricultural & Mechanical College.;

  • 授予单位 Louisiana State University and Agricultural & Mechanical College.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 1982
  • 页码 193 p.
  • 总页数 193
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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