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Flow in the matrix parallel to the fracture is ignored in this model. The absolute permeability of the fracture is assumed to be much greater than that of the reservoir matrix, resulting in the simplification that flow in the matrix is predominately perpendicular to the fracture face. The numerical model simulates multicomponent, multiphase, compressible flow through a horizontal two-dimensional porous medium which is bounded on one side by a one-dimensional fracture. This study is limited to an investigation of the behavior of the flows in and near a fracture.
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(ANL), Argonne, IL (United States) OSTI Identifier: 5317313 Report Number(s): ANL/MHD-77-4 DOE Contract Number: W-31-109-ENG-38 Resource Type: Technical Report Country of Publication: United States Language: English Subject: 30 DIRECT ENERGY CONVERSION 01 COAL, LIGNITE, AND PEAT COAL FINES COMBUSTION PRODUCTS COAL-FIRED MHD GENERATORS COMPUTER CALCULATIONS WORKING FLUIDS CHEMICAL COMPOSITION PHASE TRANSFORMATIONS SEED RECOVERY ASHES CARBONATES COMPUTER CODES EQUILIBRIUM EVAPORATION FORTRAN G CODES HYDROXIDES M CODES OPEN-CYCLE MHD GENERATORS OXIDES PHASE STUDIES PLASMA SEEDING POTASSIUM ADDITIONS SILICATES SLAGS SULFATES VAPOR CONDENSATION VAPOR PRESSURE ALLOYS CARBON COMPOUNDS CARBONACEOUS MATERIALS CHALCOGENIDES COAL DIRECT ENERGY CONVERTERS ENERGY SOURCES FLUIDS FOSSIL FUELS FUELS HYDROGEN COMPOUNDS MHD GENERATORS OXYGEN COMPOUNDS PHYSICAL PROPERTIES POTASSIUM ALLOYS PROGRAMMING LANGUAGES RECOVERY RESIDUES SILICON COMPOUNDS SULFUR COMPOUNDS THERMODYNAMIC PROPERTIES 300104* - MHD Generators- Duct Engineering & Fluid Dynamics 014000 - Coal, Lignite, & Peat- = , « lessĪuthors: Blackburn, P E Publication Date: Research Org.: Argonne National Lab. MHDGAS retains the condensate for each step, simulating flow of condensate (and gas) through the MHD system. GASCON calculates the equilibrium gas partial pressures and the quantity and composition of the condensed phases in steps of thirteen temperature and pressure combinations in which the condensate more » is removed after each step, simulating continuous slag removal from the MHD system.
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Two versions of the computer code have been written. This process, together with a normalization step, allows the elements to converge to their initial quantities. The decision to increase or decrease the oxygen pressure in this process depends on comparison of the oxygen content calculated in the gas and condensate phases with the initial amount of oxygen in the ash, coal, seed, and air. During iteration the oxygen partial pressure is incrementally changed. Calculations are iterated for gas and condensate concentrations while increasing or decreasing the total moles of elements, but keeping mole ratios constant, to achieve the desired total pressure. It is assumed that the phases are an oxide-silicate phase and a sulfate-carbonate-hydroxide phase. The codes are based on temperature-dependent equilibrium constants, mass conservation, the mass action law, and assumed ideal solution of compounds in each of two condensed phases. Lift Ya Leg Up - Spice & Company 2.Fortran IV computer codes have been written to calculate the equilibrium partial pressures of the gaseous phase and the quantity and composition of the condensed phases in the open-cycle MHD system.
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