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Untitled - Aerobib - Universidad Politécnica de Madrid

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13.5. NOTATION 307<br />

2) The phenomenon is quasi-stationary.<br />

3) Combustion takes place at constant pressure.<br />

4) The droplet temperature is uniform and equal to the boiling temperature of the<br />

fuel at ambient pressure.<br />

5) The chemical reaction takes place upon a spherical surface, named the flame<br />

front. Fuel vapours and oxygen diffuse in the stoichiometric ratio towards this<br />

flame front from which the burnt gases flow. The gases that reach the flame front<br />

react instantaneously. Thereby, on the flame front both the mass fractions of fuel<br />

vapours and of oxygen are zero.<br />

6) Only three chemical species exist, namely: fuel, oxygen and inert gases.<br />

These assumptions allow a simple analysis of the problem and lead to results<br />

which have been experimentally confirmed. Such a treatment of the problem has been<br />

applied by Godsave [19] and Spalding [3] in England, and by Penner and Goldsmith<br />

[20] in the U.S.A. Asi<strong>de</strong> from the aforementioned assumptions Godsave and Spalding<br />

also assume that transport coefficients are in<strong>de</strong>pen<strong>de</strong>nt from temperature by adopting<br />

a mean value for these coefficients. This rather arbitrary assumption reduces appreciably<br />

the suitability of the method. In fact, for the existing range of temperatures, these<br />

coefficients can vary in a ratio of ten to one. Goldsmith and Penner take into account<br />

this variation as well as that of heat capacities. The following study is mainly based<br />

on the work of these two authors but it assumes that heat capacities are in<strong>de</strong>pen<strong>de</strong>nt<br />

from temperature since their variation has no substantial influence on the results.<br />

13.5 Notation<br />

In the present study the notation used in the preceding chapter will be completed with<br />

the following (see Fig. 13.1):<br />

M = Droplet mass<br />

m = Mass flow across a closed surface surrounding the droplet.<br />

q l = Latent heat of evaporation per unit mass of fuel.<br />

r = Radial distance to the center of the droplet.<br />

v = Radial velocity of the mixture.<br />

v j = Radial velocity of species A j .<br />

v jd = Radial diffusion velocity of species A j .<br />

Y j = Mass fraction of species A j .<br />

ν = Stoichiometric ratio of oxygen mass to fuel mass.

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