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I.Panfilova, A.Pereira, S.C.Yusuf, O.Heidarov (LEMTA) A.Burnol, P.Audigan, M.Parmentier (BRGM)

Hydrodynamic analysis of spreading regimes and multi-component gas diffusion in the underground storage of radioactive wastes. I.Panfilova, A.Pereira, S.C.Yusuf, O.Heidarov (LEMTA) A.Burnol, P.Audigan, M.Parmentier (BRGM). Problematics.

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I.Panfilova, A.Pereira, S.C.Yusuf, O.Heidarov (LEMTA) A.Burnol, P.Audigan, M.Parmentier (BRGM)

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  1. Hydrodynamic analysis of spreading regimes and multi-component gas diffusion in the underground storage of radioactive wastes I.Panfilova, A.Pereira, S.C.Yusuf, O.Heidarov (LEMTA) A.Burnol, P.Audigan, M.Parmentier (BRGM)

  2. Problematics Gas mixture, composed by H2, N2, CO2, O2, SO2, etc., is accumulated in alveoli and begins to migrate in all directions caused by the segregation, dissolution and diffusion. Storage cell of type B

  3. Problematics Undercritical CO2: two-phase vertical raising Overcritical CO2: Singler-phase horizontal spreading

  4. Problematics Undercritical CO2: two-phase vertical raising Overcritical CO2: Singler-phase horizontal spreading Does it can be stopped ? Does it can be stopped ?

  5. Migration of gas • Injected gas bubble can migrate along the limited distance and be trapped for the long-term security of storage by • -structural trapping • residual gas trapping • dissolution in water • capillary forces • reactivity • The combination of these effects prevents the gas migrating more than a few kilometers from the injection site before it is fully blocked in the cap rocks.

  6. CO2 Storage Models Van der Meer : CO2 storagein saline aquifers. The dissolution rates is determined by gravity segregation and viscous displacement. Holt et al.: reservoir simulation to investigate the storage capacity defined as CO2 dissolved in formation brine. Law and Bachu showed that a similar fraction of CO2 may dissolve into the brine and travel within the slow hydrodynamic system in the aquifer Pruess et al.: CO2 storage in saline aquifers. The long-term total storage capacity could be on the order of 30 kg/m3 of aquifer volume for all trapping mechanisms. Kochina et al and Barenblatt studied analytically the capillary trapping effects.

  7. Undercritical CO2: Vertical gas raising

  8. Mathematical model of gas raising Two-phase mass balance: For each fluid phase, Darcy’s law: Initial condition: z S

  9. Segregation model Reduction to: gravity capillarity

  10. Analytical solution: diagrammatic technique Fractional flow Welge tangent Evaluation in time of multiple fronts

  11. Dynamics of bubble raising Axe vertical

  12. Bubble streatching The back velocity << The forward velocity Therefore, the bubble stretches until it reaches uniform residual gas saturation : Very different from raising in bulk water

  13. Dynamics of bubble raising Axe vertical

  14. J(S) Raising with capillary pressure

  15. Raising with Pc, Sres=0 Axe vertical

  16. Overcritical CO2: Horizontal reactive spreading

  17. Physical formulation • - Single-phase liquid. • - 2 chemical components: CO2 et H2O. • The solid is immobile and non deformable. • Fluid flow is radial. • Both components of liquid are reactive (the reaction with the solid): CO2 + 2H2O + anorthite = kaolinite + CaCO3

  18. Mathematical model C = CO2 molar concentration Reaction kinetics: Law of action mass: CO2 + 2H2O + anorthite = kaolinite + CaCO3

  19. Analytical solution stationary limit

  20. Numerical result Solid phase saturation limit of propagation for 10 years Anorthite concentration

  21. Numerical study of gas spreading Gocad ECLIPSE

  22. Vertical cross-section. Gas saturation 10 years of gas injection, 90 years without injection (natural gas migration) After 6 years of rest the gas bubble was stabilized

  23. Vertical cross-section. Water saturation

  24. Aqueous concentration of CO2

  25. Aqueous concentration of CO2

  26. Numerical study of gas spreading RSW: after 10 years of gas injection RSW: 100 years after STOP RSW: 500 years after STOP RSW: 1100 years after STOP

  27. Numerical study of gas dissolution RSW in 4 points in time (1100 years) Depth Time

  28. Proposal for 2011 • LEMTA: • Multi-component reactive diffusion-convection with gravity around a cell of radioactive waste. 3 chemical components in liquid: H2O, H2 and CO2 or air. • Model: diffusion fluxes resulting from the non-equilibrium thermodynamics. • Method: the numerical code developed in LEMTA. • 2. Macroscopic circulations in a limit volume of gas. Water surrounding the macroscopic gas bubble causes the rotational flow inside it. It may be captured only within the Brinkman model. • BRGM: • A literature review is planned to study each of 3 binary systems (CO2-H2O, CO2-H2 et H2O-H2) and calculations initiated with the binary CO2-H2S pursued. The result will be achieved with a Master student (initially planned during the first year of the project).

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