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The Implementation of NonCondensable Mass Equations Including a Dissolved Gas Source
Film Waviness Effect on the Condensation Mass Transfer of Turbulent Pipe Flow in
Combustion Modeling in Waste Tanks
42 other sections not shown
absorber air preheater analysis average axial Bingham plastic model biofilm bubble calculated capillary CFAST compared comparison computational concentration condensation convective heat transfer coolant corium correlation decreases density deposition diameter droplet drywell effect energy enhancement equation ethanol experimental data experiments fire room flow rate fluid foulant fouling factor fouling probe fouling resistance fraction frost formation function heat and mass heat exchanger heat flux heat pipe heat transfer coefficient heat transfer rate heater hydrogen increase initial inlet interface layer liner liquid film mass transfer maximum measured meniscus method mixture nozzle nucleate boiling Nusselt Nusselt number obtained ozonation parameters particles performed phase plate pool position predicted pressure drop radial RBMK reactor region Reynolds number shear stress shown in Figure shows simulations solution stack steam subcooled surface test section thermal conductivity thermoacoustic thermocouples thermopower thickness tube turbulent two-phase values vapor vertical