{"title":"CO2/brine interfacial tension for geological CO2 storage: A systematic review","authors":"Cheng Zhang , Milei Wang","doi":"10.1016/j.petrol.2022.111154","DOIUrl":null,"url":null,"abstract":"<div><p>Given that the interfacial tension (IFT) of the CO<sub>2</sub>/brine system is a critical parameter in geological CO<sub>2</sub> storage (GCS), this paper presents a systematic review of the present studies on the IFT of CO<sub>2</sub>/brine system, mainly including experimental methods, data and influencing factors.</p><p><span>IFT is caused by an imbalance of molecular forces at the interface of two immiscible fluids<span>, and the pendant drop method is considered the most convenient method to determine its value. The axisymmetric drop shape analysis (ADSA) theory derived from the Young-Laplace equation is regarded as the most advanced and accurate theory for the analysis of the results of the pendant drop measurements. The IFT of the CO</span></span><sub>2</sub><span>/brine system is determined by the temperature, pressure, salt species and salinity of the brine and the impurity of the CO</span><sub>2</sub> phase. The results indicated that the greater solubility of CO<sub>2</sub> caused by increasing temperature increase the density difference between brine and CO<sub>2</sub>, leading to an increase in the IFT. Under low-pressure conditions, the IFT decreases suddenly due to the increase in the CO<sub>2</sub> solubility and the CO<sub>2</sub><span> density with pressure. However, after reaching the supercritical state; CO</span><sub>2</sub> solubility and density hardly change with pressure, thus, IFT does not depend on the pressure. When ions are dissolved in water, the combined effect of decreased solubility of CO<sub>2</sub><span><span> in the aqueous phase, and enhanced electrostatic force and interfacial </span>ionic strength<span> gradient leads to a positive effect of the ion concentration on the IFT. The introduction of impurity gases lighter than CO</span></span><sub>2</sub> can enhance the IFT by increasing the density difference between CO<sub>2</sub> and brine. The findings of this study can help to better understand the IFT of CO<sub>2</sub>/brine systems used for geological CO<sub>2</sub> storage.</p></div>","PeriodicalId":16717,"journal":{"name":"Journal of Petroleum Science and Engineering","volume":"220 ","pages":"Article 111154"},"PeriodicalIF":0.0000,"publicationDate":"2023-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"4","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Petroleum Science and Engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0920410522010063","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"Earth and Planetary Sciences","Score":null,"Total":0}
引用次数: 4
Abstract
Given that the interfacial tension (IFT) of the CO2/brine system is a critical parameter in geological CO2 storage (GCS), this paper presents a systematic review of the present studies on the IFT of CO2/brine system, mainly including experimental methods, data and influencing factors.
IFT is caused by an imbalance of molecular forces at the interface of two immiscible fluids, and the pendant drop method is considered the most convenient method to determine its value. The axisymmetric drop shape analysis (ADSA) theory derived from the Young-Laplace equation is regarded as the most advanced and accurate theory for the analysis of the results of the pendant drop measurements. The IFT of the CO2/brine system is determined by the temperature, pressure, salt species and salinity of the brine and the impurity of the CO2 phase. The results indicated that the greater solubility of CO2 caused by increasing temperature increase the density difference between brine and CO2, leading to an increase in the IFT. Under low-pressure conditions, the IFT decreases suddenly due to the increase in the CO2 solubility and the CO2 density with pressure. However, after reaching the supercritical state; CO2 solubility and density hardly change with pressure, thus, IFT does not depend on the pressure. When ions are dissolved in water, the combined effect of decreased solubility of CO2 in the aqueous phase, and enhanced electrostatic force and interfacial ionic strength gradient leads to a positive effect of the ion concentration on the IFT. The introduction of impurity gases lighter than CO2 can enhance the IFT by increasing the density difference between CO2 and brine. The findings of this study can help to better understand the IFT of CO2/brine systems used for geological CO2 storage.
期刊介绍:
The objective of the Journal of Petroleum Science and Engineering is to bridge the gap between the engineering, the geology and the science of petroleum and natural gas by publishing explicitly written articles intelligible to scientists and engineers working in any field of petroleum engineering, natural gas engineering and petroleum (natural gas) geology. An attempt is made in all issues to balance the subject matter and to appeal to a broad readership.
The Journal of Petroleum Science and Engineering covers the fields of petroleum (and natural gas) exploration, production and flow in its broadest possible sense. Topics include: origin and accumulation of petroleum and natural gas; petroleum geochemistry; reservoir engineering; reservoir simulation; rock mechanics; petrophysics; pore-level phenomena; well logging, testing and evaluation; mathematical modelling; enhanced oil and gas recovery; petroleum geology; compaction/diagenesis; petroleum economics; drilling and drilling fluids; thermodynamics and phase behavior; fluid mechanics; multi-phase flow in porous media; production engineering; formation evaluation; exploration methods; CO2 Sequestration in geological formations/sub-surface; management and development of unconventional resources such as heavy oil and bitumen, tight oil and liquid rich shales.