Introduction
Model of two-phase transport for UHS
Governing equations
Closure equations
Hydrodynamic parameters
Numerical implementation
Simulation study of gas injection into an anticline structure
Characteristic parameter | Value | Unit |
---|---|---|
Pressure |
\(6\times 10^{6}\)
| Pa |
Density |
\(10\)
| kg/m\(^{3}\)
|
Viscosity |
\(1\times 10^{-5}\)
| Pa\(\cdot\) s |
Diffusion coefficient |
\(1\times 10^{-6}\)
| m\(^{2}\)/s |
Length | 500 | m |
Permeability | 100 | mD |
Molar mass |
\(2\times 10^{-3}\)
| kg |
Gravity acceleration | 9.81 | m/s\(^{2}\)
|
Time | 48.2 | days |
Selective technology
Analytical modeling of gas rising in a stratified reservoir
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Two-phase flow of gas and water
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Incompressible fluids
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No capillary pressure
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No diffusion
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Constant temperature
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Ideal mixing
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Phases in thermodynamic equilibrium
Numerical modeling of gas rising in a stratified reservoir
Conclusions
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A mathematical model was presented which describes the hydrodynamic effects in UHS. It considers the convective and diffusive fluxes of four chemical components in two mobile phases. Numerically, it is implemented using the open source code DuMux.
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The simulation study of gas injections into a reservoir shows some significant differences depending on the injection rate. For low injection rates, gravitational forces are dominant, and the displacement of water is uniform. However, for higher injection rates, the viscous forces become dominant, and the displacement becomes unstable. Lateral gas fingering starts to propagate below the cap rock toward the left and right boundaries of the reservoir. It has been shown that hydrogen spreads laterally, faster than methane.
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Hydrogen storage in stratified aquifers could prohibit the risk of gas losses due to lateral spreading or viscous fingering beyond the spill point. The implementation requires the “selective technology” whereby the hydrogen is injected at the bottom of the structure and produced below the cap rock. The delay in the gas rising plays a key role in this method.
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The analytical modeling of rising gas shows that downward shocks or gas accumulations occur below the first barrier. A further gas accumulation appears when the second barrier has a lower permeability than the first one. The analytical solution can be used to determine the rising velocity after passing each barrier.
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The numerical model with impermeable but spatial limited barriers also demonstrates the delayed rising of hydrogen. The displaced alignment causes a delay at each line of barriers. The spatial extent of the barriers has a considerable influence on the velocity of the rising gas.