28 research outputs found
Measurement and modelling of mass diffusion coefficients for application in carbon dioxide storage and enhanced oil recovery
Get PDFIn this work, measurements were carried out by the Taylor dispersion method [1, 2] to determine the
mutual diffusion coefficient for CO2 in water or hydrocarbon at effectively infinite dilution.
Measurements were carried out for CO2 in water, hexane, heptane, octane, decane, dodecane,
hexadecane, cyclohexane, squalane and toluene at temperatures between 298 K and 423 K with
pressures up to 69 MPa. Measurements of CO2 diffusivity in different brines were also carried out by
13C pulsed-field gradient NMR
New high-pressures vapor-liquid equilibrium data for the carbon dioxide + 2-methyl-1-propanol (isobutanol) binary system
No full textMeasurements and Modeling of High-Pressure Phase Behavior of the Carbon Dioxide + Pentan-1-ol Binary System
No full textNew high-pressures vapor-liquid equilibrium data for the carbon dioxide + 2-methyl-2-propanol binary system
No full text
Measurement and modelling of mass diffusion coefficients for application in carbon dioxide storage and enhanced oil recovery
No full textIn this work, measurements were carried out by the Taylor dispersion method [1, 2] to determine the
mutual diffusion coefficient for CO2 in water or hydrocarbon at effectively infinite dilution.
Measurements were carried out for CO2 in water, hexane, heptane, octane, decane, dodecane,
hexadecane, cyclohexane, squalane and toluene at temperatures between 298 K and 423 K with
pressures up to 69 MPa. Measurements of CO2 diffusivity in different brines were also carried out by
13C pulsed-field gradient NMR
