Beyond Henry’s law in the gas–liquid equilibrium

Carrero-Mantilla, Javier

doi:10.1007/s40828-021-00153-y

Cited by 6 publications

(2 citation statements)

References 43 publications

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“…( 14) it becomes which replaced in Eqs. ( 3) and ( 4) yields where ΔH is the enthalpy of dissolution of i, from the gas to the liquid phase [13][14][15][16].…”

Section: Gas-liquid Equilibriummentioning

confidence: 99%

Application of the van’t Hoff equation to phase equilibria

Carrero

2024

ChemTexts

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Abstractvan’t Hoff and Clausius–Clapeyron equations correspond to chemical and phase equilibria, respectively, but the Clausius–Clapeyron equation can be also a result of the application of van’t Hoff equation to the liquid–vapor or solid–vapor phase equilibrium of pure substances. Moreover, the application of van’t Hoff to gas–liquid and solid–liquid equilibrium data makes it possible to obtain enthalpies of dissolution. Examples based on published experimental data are included for all cases.

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“…( 14) it becomes which replaced in Eqs. ( 3) and ( 4) yields where ΔH is the enthalpy of dissolution of i, from the gas to the liquid phase [13][14][15][16].…”

Section: Gas-liquid Equilibriummentioning

confidence: 99%

Application of the van’t Hoff equation to phase equilibria

Carrero

2024

ChemTexts

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“…With the values for κ i , the fraction of the components in the different phases can be calculated. The exact numerical calculation of this phase composition is an elaborate step, which can be found in numerous works [21].…”

Section: Thermodynamic Modelmentioning

confidence: 99%

Dynamic Simulation of a Gas and Oil Separation Plant with Focus on the Water Output Quality

Jonach,

Haddadi,

Jordan

et al. 2023

Energies

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Gas and oil separation plants are the first main step in the production of hydrocarbon products. Depending on the properties of the recovered components from the well heads, and the physical properties in the underground rock reservoir, the plant design can vary in different ways. In mature oil and gas fields, secondary recovery methods are often used, which include the injection of large amounts of water into the underground reservoir, to induce the production flow of the wells. The handling of this water is of significant interest, in terms of production efficiency and pollution reduction, because the water comes into contact with the environment during and after recovery operations. In this work, a model of an exemplary gas and oil separation plant was created in Aspen HYSYS V10. A particular focus was placed on the modeling of oil residues in the water-bearing plant components. This model was then extended by the implementation of different process control schemes, to create a predictive model that could represent dynamic operating states in the plant components. Two different dynamic changes were then simulated using this model, to showcase the capabilities and capacities of the model.

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Bubbling in carbon dioxide aqueous solutions containing fine air bubbles

Onda

2023

Colloids and Surfaces A: Physicochemical and Engineering Aspect

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Beyond Henry’s law in the gas–liquid equilibrium

Cited by 6 publications

References 43 publications

Application of the van’t Hoff equation to phase equilibria

Application of the van’t Hoff equation to phase equilibria

Dynamic Simulation of a Gas and Oil Separation Plant with Focus on the Water Output Quality

Bubbling in carbon dioxide aqueous solutions containing fine air bubbles

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