126 results on '"Cézac, Pierre"'
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2. The solubility of H2 in NaCl brine at high pressures and high temperatures: Molecular simulation study and thermodynamic modeling
3. Solubility of H2 in water and NaCl brine under subsurface storage conditions: Measurements and thermodynamic modeling
4. Surface analyses of low carbon steel and stainless steel in geothermal synthetic Na-Ca-Cl brine saturated with CO[formula omitted]
5. Assessment of the in situ biomethanation potential of a deep aquifer used for natural gas storage.
6. An improved model for CO2 solubility in aqueous Na+–Cl−–SO42− systems up to 473.15 K and 40 MPa
7. Solubility of H2 in water and NaCl brine under subsurface storage conditions: Measurements and thermodynamic modeling
8. Figure 1 from: Ranchou-Peyruse M, Guignard M, Chiquet P, Cézac P, Ranchou-Peyruse A (2023) Assessment of the in situ biomethanation potential of a deep aquifer used for natural gas storage. ARPHA Conference Abstracts 6: e109175. https://doi.org/10.3897/aca.6.e109175
9. Assessment of the in situ biomethanation potential of a deep aquifer used for natural gas storage
10. Simulations of the Impact of Co-injected Gases on CO2 Storage, the SIGARRR Project: Processes and Geochemical Approaches for Gas-water-Salt Interactions Modeling
11. A deep continental aquifer downhole sampler for microbiological studies
12. Kinetic factors affecting jarosite formation at room and high temperatures
13. Comparative study of three H2 geological storages in deep aquifers simulated in high pressure reactors.
14. Thermal and volumetric properties of complex aqueous electrolyte solutions using the Pitzer formalism – The PhreeSCALE code
15. Model for the DSC thermograms of the melting of ideal binary solutions
16. Biological, geological and chemical effects of oxygen injection in underground gas storage aquifers in the setting of biomethane deployment
17. A New Pitzer Parameterization for the Binary NaOH–H2O and Ternary NaOH–NaCl–H2O and NaOH–LiOH–H2O Systems up to NaOH Solid Salt Saturation, from 273.15 to 523.15 K and at Saturated Vapor Pressure
18. Geological Storage of Hydrogen in Deep Aquifers – an Experimental Multidisciplinary Study
19. Experimental measurements and thermodynamic modeling of CO2 solubility in the NaCl-Na2SO4-CaCl2-MgCl2 system up to 150 °C and 200 bar
20. Microbial Diversity Under the Influence of Natural Gas Storage in a Deep Aquifer
21. Thermodynamic Modeling of Mutual Solubilities in Gas-Laden Brines Systems Containing CO2, CH4, N2, O2, H2, H2O, NaCl, CaCl2, and KCl: Application to Degassing in Geothermal Processes
22. Experimental studies of solubility of elemental sulphur in supercritical carbon dioxide
23. Experimental Measurements of CO2 Solubility in Aqueous MgCl2 Solution at Temperature between 323.15 and 423.15 K and Pressure up to 20 MPa
24. Three thermodynamic paths to describe solid fugacity: Application to sulphur precipitation from supercritical natural gas
25. Elemental sulphur deposition in natural gas transmission and distribution networks
26. Research on the injection of new gases in underground methane storage systems in deep aquifers.
27. Experimental Study of Carbon Dioxide Solubility in Sodium Chloride and Calcium Chloride Brines at 333.15 and 453.15 K for Pressures up to 40 MPa
28. Modelling solubility of solid sulphur in natural gas
29. Experimental Measurements of CO2 Solubility in Aqueous MgCl2 Solution at Temperature between 323.15 and 423.15 K and Pressure up to 20 MPa.
30. Experimental Measurement of CO2 Solubility in Aqueous Na2SO4 Solution at Temperatures between 303.15 and 423.15 K and Pressures up to 20 MPa
31. Experimental Study of the Liquid Vapour Equilibrium of the System Water‐CO 2 ‐O 2 ‐NO x Under Pressure at 298 K
32. Experimental Determination of CO2Solubility in Brines At High Temperatures and High Pressures and Induced Corrosion of Materials in Geothermal Equipment
33. Geological gas‐storage shapes deep life
34. Experimental determination of CO2 solubility in brines at high temperatures and high pressures and induced corrosion of materials in geothermal equipment
35. Experimental Measurements of CO2Solubility in Aqueous MgCl2Solution at Temperature between 323.15 and 423.15 K and Pressure up to 20 MPa
36. Experimental measurements of CO2 solubility in salt solutions at high temperatures and high pressures
37. Experimental Measurements of Carbon Dioxide Solubility in Na–Ca–K–Cl Solutions at High Temperatures and Pressures up to 20 MPa
38. Mesures expérimentales de la solubilité du CO2 dans des solutions salées à hautes températures et à hautes pressions
39. Environmentally Friendly Process for Producing Magnesium-Enriched Salt
40. Experimental Study of Carbon Dioxide Solubility in Sodium Chloride and Calcium Chloride Brines at 333.15 and 453.15 K for Pressures up to 40 MPa.
41. MODELING THE EXCESS PROPERTIES OF AQUEOUS SYSTEMS WITH THE PITZER MODEL: APPLICATION TO THE NaOH-H2O BINARY SYSTEM
42. A new set of Pitzer interaction parameters to describe solution properties and solid-liquid equilibria in the Li-Ca-Cl-H 2 O system at 298.15 K
43. PhreeSCALE: a new numerical tool to compute the thermal and volumetric properties of brines with the Pitzer model
44. Considerations about the building of a thermodynamic database for the chemical description of highly saline systems
45. Experimental Measurement of CO2Solubility in Aqueous CaCl2Solution at Temperature from 323.15 to 423.15 K and Pressure up to 20 MPa Using the Conductometric Titration
46. Solution properties and salt-solution equilibria in the H-Li-Na-K-Ca-Mg-Cl-H2O system at 25 °C: A new thermodynamic model based on Pitzer's equations
47. Experimental Measurement of CO2 Solubility in Aqueous CaCl2 Solution at Temperature from 323.15 to 423.15 K and Pressure up to 20 MPa Using the Conductometric Titration
48. Experimental Data and Modeling of Solution Density and Heat Capacity in the Na–K–Ca–Mg–Cl–H2O System up to 353.15 K and 5 mol·kg–1 Ionic Strength
49. Lithium extraction from brines : an integrated method combining thermodynamic modelling and experiments
50. Estimation of Pitzer interaction parameters from heat capacity and osmotic coefficient for the NaOH-H2O system at temperatures from 0 to 150°C and concentrations up to NaOH(s) saturation
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