This User Manual provides instructions on how to use the PFLOTRAN-OGS flow models:
Gas-Water for CO2 Storage in saline aquifer (GAS_WATER).
Three-component Multi-Gas for CO2 Storage in depleted gas fields (COMP3).
Four-component Multi-Gas for CO2 Storage in depleted hydrocarbon fields in cases of small quantities of residual oil (COMP4).
Multi-component for CO2 Storage in more complex depleted hydrocarbon fields (COMP).
Black-Oil (BLACK_OIL), Todd-Longstaff (TODD_LONGSTAFF), Solvent (SOLVENT_TL) and Oil-Water (TOIL_IMS), for other hydrocarbon applications.
GAS_WATER, BLACK_OIL, TODD_LONGSTAFF and SOLVENT_TL can run both in isothermal and thermal mode. At present COMP3, COMP4, and COMP can account for time-constant temperature-gradient effects, but run only in isothermal mode.
The multi component mode (COMP) also describes a flow model flow model consiting of water and any number of additional compnents.
Describes a flow model with OIL, GAS, SOLVENT and WATER. Note that SOLVENT will often be CO2, but this is not a requirement. The SOLVENT and GAS components share the gas phase, both may dissolve in the oil, and the solvent component may dissolve in the aqueous phase.
Describes a flow model with, GAS, SOLVENT and WATER. Note that SOLVENT will often be CO2, but this is not a requirement. The SOLVENT and GAS components share the reservoir vapour phase, and the solvent component may dissolve in the aqueous phase. This is a generalisation of the GAS_WATER mode to handle carbon storage in depleted gas reservoirs in which both original reservoir gas (GAS component) and injected CO2 (SOLVENT) are present.
Similar to COMP4 but with no oil data to specify. The SOLVENT data can be set with a Span Wagner CO2 properties database as in GAS_WATER mode. The gas properties can be set with a PVDG properties table.
The Gas-water module (GAS_WATER) describes a two-phase flow model. In this case each phase may contain both components: the aqueous phase may contain dissolved gas, and the gas phase may contains vapourised water. The module solves a molar balance equation for each component and an energy equation to account for thermal effects. For more details see the Mathematical formulation of Gas-Water in the theory guide.
The Black Oil Model is a common fluid treatment in reservoir simulation. In this treatment, gas is allowed to dissolve in the reservoir oil phase. The amount of dissolved gas in the oil is parameterized by the oil saturation pressure, commonly known as the bubble point. Oil properties such as the formation volume factor (volume of oil at reservoir conditions/volume of oil at surface conditions), enthalpy and viscosity will generally be functions of pressure and bubble point. See Mathematical formulation of the Black Oil Model in the theory guide.
The simple Todd-Longstaff model is suitable for cases in which the reservoir is undersaturated with no free gas. In this case the solvent is represented by the gas phase. See Mathematical formulation of the simple Todd-Longstaff Model in the theory guide.
The Solvent model is an extension of black oil model which adds an additional solvent phase, commonly used to represent an injected fluid such as carbon dioxide which is fully or partially miscible with the oil. See Mathematical formulation of the Solvent Model in the theory guide.
The Thermal Oil Immiscible (TOIL_IMS) module describes a two-phase flow model, in which the oil and water phases are considered immiscible. The module solves a molar balance equation for each phase and an energy equation to account for thermal effects. Each phase is assumed to contain only one component: the water phase contains 100% H2O, the oil CO2 phase contains 100% of a user-defined oil component. For more details see the Mathematical formulation of toil-ims in the theory guide.
In the above flow models, if the ISOTHERMAL mode has not been selected, temperature variation will be modeled for each cell. Within a single cell, the fluids and rock are assumed to be in thermal equilibrium, and to share the same cell temperature. In isothermal mode the energy equation is not solved and the temperature is assumed not to vary with time. The thermal option is not currently available for COMP3, COMP4 and COMP.