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Untitled - Aerobib - Universidad Politécnica de Madrid

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314 CHAPTER 13. COMBUSTION OF LIQUID FUELS<br />

The solution of Eq. (13.44) must satisfy another additional condition. In fact,<br />

the mass fraction of oxygen must tend to the value Y 3∞ corresponding to the composition<br />

of the atmosphere surrounding the droplet at great distance from the same<br />

r → ∞ : Y 3 → Y 3∞ . (13.46)<br />

This equation will be used in <strong>de</strong>termining the burning velocity m of the droplet.<br />

13.9 Combustion velocity of the droplet. Temperature<br />

and position of the flame<br />

From the preceding paragraph it results that the solution of the combustion problem<br />

of a droplet reduces to the following:<br />

1) The integration of the system of differential equations<br />

4πr 2 λ dT ∫ (<br />

T<br />

∫ )<br />

Ts<br />

dr − m c p1 dT =m q l − c p1 dT , (13.32)<br />

T 0<br />

T 0<br />

4πr 2 ρD 12<br />

dY 1<br />

dr = − m(1 − Y 1), (13.42)<br />

for the <strong>de</strong>termination of temperature T and mass fraction Y 1 of the fuel vapours<br />

within the interior region r s ≤ r ≤ r l , with the two boundary conditions<br />

r = r s : T = T s , (13.33)<br />

r = r − l<br />

: Y 1 = 0. (13.43)<br />

2) The integration of the differential equations<br />

4πr 2 λ dT ∫ (<br />

T<br />

dr − m c p dT =m q l − q r −<br />

T 0<br />

with boundary conditions<br />

∫ Ts<br />

T 0<br />

c p1 dT<br />

)<br />

, (13.36)<br />

4πr 2 ρD 23<br />

dY 3<br />

dr =m(ν + Y 3), (13.44)<br />

r →∞ : T →T ∞ , (13.38)<br />

r =r + l<br />

: Y 3 =0, (13.45)<br />

for the <strong>de</strong>termination of temperature and mass fraction Y 3 of oxygen within the<br />

exterior region r ≥ r l .

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