By Prof. Dr. L. P. Yarin, Prof. Dr. G. Hetsroni (auth.)
Combustion of Two-Phase Reactive Media addresses the advanced phenomena fascinated about the burning of reliable and liquid fuels. actually, the multiplicity of phenomena attribute of combustion of two-phase media be sure the contents. the 3 components take care of: the dynamics of a unmarried particle; combustion wave propagation in two-phase reactive media; and thermal regimes of combustion reactors. The e-book generalizes the results of a number of investigations of ignition and combustion a superior debris, droplets and bubbles, combustion wave propagation in heterogeneous reactive media, balance of combustion of two-phase media, in addition to the thermal regimes of high-temperature combustion reactors. It merges findings from the authors’ investigations into difficulties of two-phase flows and fabric from graduate-level classes they educate at Technion-Israel Institute of Technology.
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Additional resources for Combustion of Two-Phase Reactive Media
Q)/a)/qe is the Spalding transfer number for non burning and burning droplet, cp is the specific heat of gas-vapor mixture, q and qe are the heat of combustion and latent heat of vaporization, Co,,,, the ambient oxygen concentration, a the stoichiometric oxidizer-to-fuel mass ratio, Ts and Too are the droplet surface temperature that corresponds to saturated pressure under conditions of thermodynamic equilibrium and ambient temperature. One should note that the drag of a vaporizing drop depends also on the viscosity ratio of the inner and outer fluids.
Fluid Mech. 16: 161176 Moore DW (1965) The velocity of rise of distorted gas bubbles in a liquid of small viscosity. J. Fluid Mech. 23: 749-766 Morsi SA, Alexander AJ (1972) An investigation of particle trajectories in two-phase flow systems. 1. Fluid Mech. 55: 193-208 Muggia A (1956) Speed of evaporation and drag coefficient for a droplet in a gas stream. Aerotecnica Roma 36: 127-131 Natarajan R (1973) Experimental drag coefficients for evaporating and burning drops at elevated pressure. Combust.
11 Streamlines of the flow inside and outside the vaporizing droplet. 1 1 10 100 Aoo Fig. 12 The normalized drag force versus radial velocity. 1 Drag of solid particles, droplets and bubbles The streamlines of the flows inside and outside the vaporizing droplet are shown in Fig. 11. These data correspond to the case where the radial velocity distribution has a maximum at e = n. The circulation of the fluid inside the droplet (recalling Hill's spherical vortex) is due to the liquid-gas interaction at the interface.