1992
DOI: 10.1029/91wr02526
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Numerical modeling of steam injection for the removal of nonaqueous phase liquids from the subsurface: 1. Numerical formulation

Abstract: A multidimensional integral finite difference numerical simulator is developed for modeling the steam displacement of nonaqueous phase liquid (NAPL) contaminants in shallow subsurface systems. This code, named STMVOC, considers three flowing phases, gas, aqueous, and NAPL; and three mass components, air, water, and an organic chemical. Interphase mass transfer of the components between any of the phases is calculated by assuming local chemical equilibrium between the phases, and adsorption of the chemical to t… Show more

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Cited by 176 publications
(72 citation statements)
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“…Gas-phase enthalpy and internal energy are computed from component vapor quantities and gas-phase mass fractions [Falta et al 1990a], according to Equations (4.6.1) and (4.6.2). Water vapor enthalpy is computed from the steam table formulations as a function of temperature and pressure, according to Equation (4.6.3).…”
Section: Gas-phase Enthalpy and Internal Energymentioning
confidence: 99%
“…Gas-phase enthalpy and internal energy are computed from component vapor quantities and gas-phase mass fractions [Falta et al 1990a], according to Equations (4.6.1) and (4.6.2). Water vapor enthalpy is computed from the steam table formulations as a function of temperature and pressure, according to Equation (4.6.3).…”
Section: Gas-phase Enthalpy and Internal Energymentioning
confidence: 99%
“…These models show that viscous gas transport can be caused by a variety of processes including the injection and extraction of air or vapor [e.g. Massmann, 1989;Falta et al, 1992], the volatilization of organic compounds [e.g., Falta et al, 1989;Mendoza and Frind, 1990;Gaganis et al, 2004], sustained underpressurization relative to atmospheric conditions in basements of buildings and the adjacent sediments [e.g., Hers et al, 2002;Abreu and Johnson, 2005], barometric pumping [e.g., Massmann and Farrier, 1992], displacement due to infiltrating recharge water [e.g., Celia and Binning, 1992], and temperature changes [e.g., White, 1995].…”
mentioning
confidence: 99%
“…It can also been seen from Table 2 that with the increase of steam quality and overheated degree, the specific heat enthalpy, the specific heat, and the latent heat of vaporization increase simultaneously, therefore the region for steam to reduce the oil viscosity is increasingly larger, more and more oil with high mobility comes into the high-temperature regions with high oil relative permeability, and hence the good production performance of cyclic superheated steam injection can be expected (Falta et al, 1992;Li et al, 2012).…”
Section: Reservoir Engineering Analysismentioning
confidence: 94%