Abstract

When the concentration of a gas exceeds the equilibrium concentration in a liquid, the gas–liquid system is referred as a supersaturated system. The supersaturation can be achieved by either changing the pressure and/or temperature of the system. The gas from a supersaturated liquid escapes either through bubble nucleation that usually occurs on solid surface and/or gas diffusion through the gas–liquid interface. The bubble nucleation requires a minimum threshold supersaturation. A waiting time is required to observe whether the applied supersaturation is sufficient to initiate bubble nucleation. When the supersaturation is not sufficient to cause bubble nucleation, some or all of the supersaturated gas may diffuse out from the liquid through the gas–liquid interface before further reducing the pressure in order to increase the supersaturation. In this article, using Fick’s second law of diffusion and Henry’s law, an analytical method is proposed to estimate the level of supersaturations generated in three gas–liquid systems at different step-down pressures. Characteristic times of the gas–liquid systems were estimated to validate whether the waiting times used in this study are in accordance with the semi-infinite diffusion model used to estimate the supersaturations generated.

Highlights

  • IntroductionA supersaturated solution can be achieved by changing either the temperature and/or pressure of the system [1,2]

  • A gas–liquid system is referred to as supersaturated when the concentration of the solute phase exceeds the equilibrium concentration in the solvent phase.A supersaturated solution can be achieved by changing either the temperature and/or pressure of the system [1,2]

  • We present a simple analytical method developed based on Fick’s second law of diffusion and Henry’s law to estimate the supersaturations generated in three gas–liquid systems (CO2 -water, CH4 -water, and N2 -water) with two step-down pressures (100 and 500 mbar)

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Summary

Introduction

A supersaturated solution can be achieved by changing either the temperature and/or pressure of the system [1,2]. The degree of supersaturation can be described by chemical potential (μi ), which represents the deviation from equilibrium at a given temperature and pressure for a component i. For a component i in a mixture, the chemical potential in an isothermal–isobaric ensemble is given by:. T is the temperature, P is the pressure, j refers to the number of remaining components, and xi is the molar fraction of the ith component in the mixture [3]. The change in chemical potential of the component i (∆μi ) w.r.t. temperature and pressure is >0. Depending on whether the CO2 exsolution proceeds with or without bubble nucleation, the pressure response and relative permeability characteristics of the fluids in

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