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On the Formation of Nitrogen Oxides During the Combustion of ...

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4 Numerical Modeling and Simulation<br />

In addition to <strong>the</strong> assumptions made for <strong>the</strong> single droplet model, <strong>the</strong> following<br />

simplifications are introduced to achieve an analytical solution with <strong>the</strong><br />

D² law: The temperature in <strong>the</strong> droplet is homogeneous and equal to <strong>the</strong> temperature<br />

at <strong>the</strong> droplet surface T S . The problem is quasi-steady, i.e. partial<br />

derivatives in time ∂/∂t vanish. Pr<strong>of</strong>iles <strong>of</strong> temperature and mass fraction are<br />

assumed to be in steady state at each time t and droplet radius R(t ). This implies<br />

that <strong>the</strong> droplet radius changes slowly compared to <strong>the</strong> transport <strong>of</strong> heat<br />

and mass [298, 443].<br />

The transport <strong>of</strong> mass can be written for a water droplet as<br />

ṁ H2 O<br />

A<br />

= ρ dY H2 O<br />

g D H2 O,air + ṁ<br />

dr A Y H 2 O, (4.64)<br />

where ṁ H2 O/A is <strong>the</strong> mass flux <strong>of</strong> water in kg m −2 s −1 , ṁ/A <strong>the</strong> total mass flux,<br />

D H2 O,air <strong>the</strong> diffusion coefficient <strong>of</strong> water in air, ρ g <strong>the</strong> density <strong>of</strong> <strong>the</strong> humid<br />

air, and Y H2 O <strong>the</strong> mass fraction <strong>of</strong> water. The area A reflects <strong>the</strong> droplet surface<br />

with A = 4πR 2 . The mass flow <strong>of</strong> vaporizing water ṁ H2 O is equal to <strong>the</strong> total<br />

mass flow ṁ, as air is insoluble in water in a first estimate. The mass flow<br />

ṁ is constant in space, as a quasi-steady state assumption was postulated.<br />

The mass flow value is generally defined as positive, if water vaporizes and <strong>the</strong><br />

droplet shrinks.<br />

Heat transfer is described by:<br />

(<br />

d<br />

r 2 ṁ )<br />

dr A c pT − d dr<br />

(<br />

r 2 λ dT )<br />

= 0. (4.65)<br />

dr<br />

As <strong>the</strong> vaporization mass flow ṁ H2 O in Equation (4.65) is linear in R(t ) and<br />

accordingly in D, <strong>the</strong> mass fraction Y H2 O,S and droplet temperature T S at <strong>the</strong><br />

droplet surface (on <strong>the</strong> gas side) are independent <strong>of</strong> time t for this simplified<br />

validation model. Thus, <strong>the</strong> droplet diameter is<br />

D 2 = D 2 0 − k t , (4.66)<br />

where D 0 is <strong>the</strong> initial droplet diameter at t = 0 and k <strong>the</strong> vaporization rate<br />

[244, 443, 461]. Equation (4.66) is known as <strong>the</strong> D² law. It is used only within<br />

this section (Chap. 4.6) for validation purposes but not for any fur<strong>the</strong>r scientific<br />

studies. Equation (4.67) fur<strong>the</strong>r clarifies <strong>the</strong> definition <strong>of</strong> k:<br />

k =− d (D 2 )<br />

dt<br />

=−2ḊD = 2ṁ H 2 O<br />

= const. (4.67)<br />

ρ l πR(t )<br />

144

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