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Related Concept Videos

Comparing Intermolecular Forces: Melting Point, Boiling Point, and Miscibility02:34

Comparing Intermolecular Forces: Melting Point, Boiling Point, and Miscibility

Intermolecular forces are attractive forces that exist between molecules. They dictate several bulk properties, such as melting points, boiling points, and solubilities (miscibilities) of substances. Molar mass, molecular shape, and polarity affect the strength of different intermolecular forces, which influence the magnitude of physical properties across a family of molecules.
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Distillation is a separation technique that takes advantage of the boiling point properties of disparate elements in a mixture. To perform distillation, we begin by heating a miscible mixture of two liquids with a significant difference in boiling points (at least 20°C). As the solution heats up and reaches the bubble point of the more volatile component, some molecules of the more volatile component transition into the gas phase and travel upward into the condenser, which is a glass tube with...
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A pressure-composition phase diagram explicitly describes the behavior of an ideal solution of two volatile liquids under varying pressures and compositions. A pressure-composition diagram has two main curves. The bubble point curve represents the plot of pressure versus liquid mole fraction. It indicates the pressure at which the first bubble of vapor forms from the liquid phase as the system pressure decreases.The dew point curve is the pressure versus vapor mole fraction. It indicates the...
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Nonideal liquid solutions, also known as real solutions, do not strictly follow Raoult's law. Raoult's law is a rule of thumb in physical chemistry. However, not all mixtures adhere to this law due to varying molecular interactions. For example, in an acetone/chloroform solution, the individual vapor pressures of the components are lower than expected, resulting in a total vapor pressure below that predicted by Raoult's law, causing a negative deviation.On the other hand, in an ethanol/water...
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The temperature-composition phase diagram of two solids, A and B, which are immiscible in the solid phase but form miscible liquids, shows that when the temperature is low, these two exist as separate, pure solids (A and B). As the temperature increases, they transition into a single-phase liquid solution where A and B coexist. Moving from point a1 to a2 in the phase diagram, the composition changes such that solid B begins to separate from the solution, enriching the remaining liquid with A.

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Updated: Jul 18, 2026

Phase Diagram Characterization Using Magnetic Beads as Liquid Carriers
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Predicting miscibility of binary liquids from small cluster QCE calculations.

Johannes Ingenmey1, Michael von Domaros1, Barbara Kirchner1

  • 1Mulliken Center for Theoretical Chemistry, Universität Bonn, Beringstr. 4, D-53115 Bonn, Germany.

The Journal of Chemical Physics
|April 24, 2017
PubMed
Summary

The quantum cluster equilibrium method accurately predicts solvent mixing behavior for acetone-based systems. While effective for many binary solvent mixtures, it shows limitations with water-containing systems.

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Area of Science:

  • Physical Chemistry
  • Computational Chemistry
  • Thermodynamics

Background:

  • Modeling molecular solvent mixtures is crucial for understanding chemical processes.
  • Accurate prediction of thermodynamic properties like Gibbs energy of mixing is essential.
  • Existing methods often require extensive experimental data or high computational cost.

Purpose of the Study:

  • To apply the quantum cluster equilibrium method to model binary molecular solvent systems.
  • To minimize computational effort and experimental input for solvent mixture modeling.
  • To evaluate the method's accuracy for miscible and immiscible solvent pairs.

Main Methods:

  • Utilized the quantum cluster equilibrium method with small cluster sizes (n=3).
  • Employed the low-cost PBEh-3c functional for cluster optimization.
  • Approximated empirical parameters using linear interpolation, reducing reliance on binary system data.

Main Results:

  • Thermodynamic functions of pure liquids showed good agreement with experimental data.
  • Achieved high accuracy (≈0.25 kJ/mol) for Gibbs energy of mixing in non-water systems.
  • Correctly predicted mixing behavior for acetone/acetonitrile, acetone/benzene, and acetone/water systems.
  • Accurately predicted the immiscibility of benzene/water, with a minor error at high benzene concentrations.

Conclusions:

  • The quantum cluster equilibrium method, even with approximations and small cluster sets, effectively predicts mixing behavior for acetone-based binary solvent systems.
  • The approach demonstrates potential for reducing experimental data requirements in solvent mixture modeling.
  • Further refinement may be needed for accurate modeling of water-containing systems using small clusters.