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O'Rourke, P.J.; Marks, M.D.
Organisation for Economic Co-Operation and Development, Nuclear Energy Agency - OECD/NEA, Le Seine Saint-Germain, 12 boulevard des Iles, F-92130 Issy-les-Moulineaux (France)1996
Organisation for Economic Co-Operation and Development, Nuclear Energy Agency - OECD/NEA, Le Seine Saint-Germain, 12 boulevard des Iles, F-92130 Issy-les-Moulineaux (France)1996
AbstractAbstract
[en] 1 - Description of program or function: LDEF-SS solves the equations for the two-phase fluid flow in spray dryers. It calculates, by a particle method, the dynamics and vaporization of a single component liquid spray. The spray is fully-coupled to a two-component gas, consisting of an inert species and the vapor of the liquid. The effects of drop collisions and coalescence are included. The geometry is spatially two-dimensional and axisymmetric, and swirling motion is permitted about the dryer axis. A wide variety of dryer parameters, such as dryer size and geometry and atomizer size and speed, and operating conditions, such as gas-flow rates and temperatures, can be specified by user-supplied parameters. Program output includes contour, vector, and spray plots, supplemented by numerical results. 2 - Method of solution: The equations for a single-component liquid moving and evaporating in a two-component gas composed of air and the vapor of the liquid are solved by finite-difference methods. LDEF-SS incorporates the basic methodology of the stochastic parcel (SP) method, as well as many other features of the numerical solution procedure of Dukowicz, in conjunction with the Implicit Continuous-fluid Eulerian (ICE) method. An algorithm was added to calculate the effects of drop collisions. The ordinary differential equations governing the changes in drop properties are approximated by first-order methods. The finite-difference equations for the gas- phase properties are obtained by a control-volume derivation. An eddy diffusivity approximation is used to calculate the turbulent transport of mass, momentum, and energy in the gas. 3 - Restrictions on the complexity of the problem: LDEF-SS does not calculate the gas-phase transport of sulfur dioxide and its dissolution and reaction with the liquid
Primary Subject
Source
16 Apr 1996; [html]; Available on-line: http://www.nea.fr/abs/html/ests0463.html; Country of input: International Atomic Energy Agency (IAEA); 5 refs.
Record Type
Miscellaneous
Literature Type
Software
Country of publication
AIR, ALGORITHMS, APPROXIMATIONS, AXIAL SYMMETRY, COALESCENCE, COMPUTER PROGRAM DOCUMENTATION, DESULFURIZATION, DIFFERENTIAL EQUATIONS, DRYERS, EVAPORATION, FINITE DIFFERENCE METHOD, FLUE GAS, GAS FLOW, GEOMETRY, L CODES, LIQUIDS, SPRAYS, STOCHASTIC PROCESSES, SULFUR DIOXIDE, TWO-DIMENSIONAL CALCULATIONS, TWO-PHASE FLOW, VAPORS, WEBSITES
CALCULATION METHODS, CHALCOGENIDES, CHEMICAL REACTIONS, COMPUTER CODES, DOCUMENT TYPES, EQUATIONS, FLUID FLOW, FLUIDS, GASEOUS WASTES, GASES, ITERATIVE METHODS, MATHEMATICAL LOGIC, MATHEMATICAL SOLUTIONS, MATHEMATICS, NUMERICAL SOLUTION, OXIDES, OXYGEN COMPOUNDS, PHASE TRANSFORMATIONS, SULFUR COMPOUNDS, SULFUR OXIDES, SYMMETRY, WASTES
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