Experimental measurement and thermodynamic prediction of CO2 solubility in water-based drilling fluids under high-temperature and high-pressure conditions

Abstract During deep and ultra-deep drilling, CO 2 influx can alter gas–liquid phase partitioning in water-based drilling fluids and thereby affect wellbore multiphase-flow and pit-volume responses. To improve the description of this behavior, CO 2 solubility was measured for three field KCl-based polysulfonate water-based drilling fluids over 30–150 °C and 10–90 MPa using an equilibrium liquid-sampling method. A fugacity–activity framework was then established by combining the Peng–Robinson equation of state, a pressure-corrected Henry term, electrolyte activity corrections, and an empirical polymer contribution. The experimental results show that CO 2 solubility increases nonlinearly with pressure and decreases with temperature. The three formulations exhibit different solubilities; the lower solubility of the formulation containing 15% KCl is consistent with salting-out, although the simultaneous variation in polymers, asphaltic additives, and suspended solids prevents the contribution of salt from being isolated independently. For the three tested fluids, the model gives mean absolute percentage errors of 2.72%, 2.49%, and 5.03%, with R² values of 0.9891, 0.9954, and 0.9777, respectively. An engineering wellbore simulation was further used to illustrate how CO 2 dissolution/exsolution can delay mud-pit volume gain during gas influx. Because the case-study reservoir conditions (175 °C and 172 MPa) exceed the experimental validation envelope, this simulation is interpreted as an extrapolative engineering illustration rather than independent field validation. Accordingly, the proposed model is presently validated only for the three tested KCl-based water-based drilling-fluid systems within 30–150 °C and 10–90 MPa. The results provide experimental data and an engineering-oriented thermodynamic correlation for assessing CO 2 dissolution effects in deep-well well-control calculations.

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Publication Details

Journal
Journal of Engineering and Applied Science
Published
2026-09-01
DOI
https://doi.org/10.1186/s44147-026-01201-5
Primary Topic
Drilling and Well Engineering
Type
article
Field-Weighted Citation Impact
0.00

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article

Experimental measurement and thermodynamic prediction of CO2 solubility in water-based drilling fluids under high-temperature and high-pressure conditions

Xiaoke Ye, Deng Guangdong, Ergang Zhang, Haikang He et al.
Journal of Engineering and Applied Science
Drilling and Well Engineering
article

Experimental measurement and thermodynamic prediction of CO2 solubility in water-based drilling fluids under high-temperature and high-pressure conditions

Xiaoke Ye, Deng Guangdong, Ergang Zhang, Haikang He, Zhicheng Zhang, Zhiqiang Wang, Yang Ke
article en

Abstract

Abstract During deep and ultra-deep drilling, CO 2 influx can alter gas–liquid phase partitioning in water-based drilling fluids and thereby affect wellbore multiphase-flow and pit-volume responses. To improve the description of this behavior, CO 2 solubility was measured for three field KCl-based polysulfonate water-based drilling fluids over 30–150 °C and 10–90 MPa using an equilibrium liquid-sampling method. A fugacity–activity framework was then established by combining the Peng–Robinson equation of state, a pressure-corrected Henry term, electrolyte activity corrections, and an empirical polymer contribution. The experimental results show that CO 2 solubility increases nonlinearly with pressure and decreases with temperature. The three formulations exhibit different solubilities; the lower solubility of the formulation containing 15% KCl is consistent with salting-out, although the simultaneous variation in polymers, asphaltic additives, and suspended solids prevents the contribution of salt from being isolated independently. For the three tested fluids, the model gives mean absolute percentage errors of 2.72%, 2.49%, and 5.03%, with R² values of 0.9891, 0.9954, and 0.9777, respectively. An engineering wellbore simulation was further used to illustrate how CO 2 dissolution/exsolution can delay mud-pit volume gain during gas influx. Because the case-study reservoir conditions (175 °C and 172 MPa) exceed the experimental validation envelope, this simulation is interpreted as an extrapolative engineering illustration rather than independent field validation. Accordingly, the proposed model is presently validated only for the three tested KCl-based water-based drilling-fluid systems within 30–150 °C and 10–90 MPa. The results provide experimental data and an engineering-oriented thermodynamic correlation for assessing CO 2 dissolution effects in deep-well well-control calculations.

Journal of Engineering and Applied ScienceVol. 73(1)
China University of Petroleum, East China (CN), PetroChina Southwest Oil and Gas Field Company (China)
PetroChina Company Limited
Clean water and sanitation
Openalex Percentile: Top 15%
Drilling and Well Engineering
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