ECO2N V2.0: A TOUGH2 fluid property module for modeling CO2‐H2O‐NACL systems to elevated temperatures of up to 300°C. Issue 2 (1st August 2016)

• Record Type: Journal Article
• Authors: Pan, Lehua; Spycher, Nicolas; Doughty, Christine; Pruess, Karsten
• Is Part Of: Greenhouse gases. Volume 7:Issue 2(2017)
• Page Start: 313
• Page End: 327
• Publication Date: 2016-08-01
• Subjects: numerical simulator -- elevated temperature -- fluid property -- geological carbon sequestration -- CO2‐brine -- CO2‐based EGS; Greenhouse gases -- Periodicals; Greenhouse gas mitigation -- Periodicals; 363.7387405
• DOI: 10.1002/ghg.1617
• Languages: English
• ISSNs: 2152-3878

Abstract

Abstract: We have improved ECO2N, the TOUGH2 fluid property module of the CO2 ‐H2 O‐NaCl system. The major enhancements include: (i) the upper temperature limit is increased from 110 to about 300°C; (ii) the thermophysical properties of the CO2 ‐rich phase are more accurately calculated as a non‐ideal mixture of CO2 and H2 O; (iii) the approach to calculate the specific enthalpy of dissolved CO2 has been improved to make the code more robust in modeling phase transitions under non‐isothermal conditions; and (iv) more sophisticated models for effective heat conductivity of formations saturated with supercritical CO2 have been provided. The new module includes a comprehensive description of the thermodynamic and thermophysical properties of H2 ONaClCO2 mixtures, that reproduces fluid properties largely within experimental error for the temperature, pressure and salinity conditions 10°C < T < 300°C, P < 600 bar, and salinity up to halite saturation. This includes density, viscosity, and specific enthalpy of fluid phases as functions of temperature, pressure, and composition, as well as partitioning of mass components H2 O, NaCl and CO2 among the different phases. ECO2N with the TOUGH2 reservoir simulator can be applied to a wide range of problems in geologic sequestration of CO2 in saline aquifers, and in enhanced geothermal reservoirs. ECO2N can describe both sub‐ and supercritical states of CO2, but applications that involve subcritical conditions are limited to systems in which there is no change of phase between liquid and gaseous CO2, and in which no mixtures of liquid and gaseous CO2 occur. © 2016 Society of Chemical Industry and John Wiley & Sons, Ltd.