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

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4.3 Modeling <strong>of</strong> Ignition<br />

Hence, <strong>the</strong> characteristic time scale <strong>of</strong> ∆t = 1.0ms utilized for <strong>the</strong> time between<br />

heat introduction and extraction is reasonable 4 for an investigated<br />

droplet diameter <strong>of</strong> D 0 = 100µm.<br />

As for <strong>the</strong> geometrical parameters, <strong>the</strong> total volume for heat introduction is<br />

optimized for a safe ignition and set to V in = 2.0mm 3 . For heat extraction,<br />

V ex = 20.0 mm 3 is chosen in order to remove heat from a well-spread region <strong>of</strong><br />

exhaust gas outside <strong>of</strong> <strong>the</strong> burning droplet (cf. Fig. 4.3). The particular pr<strong>of</strong>iles<br />

depicted in Figure 4.3 use values <strong>of</strong> r m,in = 0.8mm and r m,ex = 1.4 mm for <strong>the</strong><br />

mean radius. The solid line shows <strong>the</strong> introduced heat when ˙q v<br />

∣<br />

∣rm<br />

= ˙q v,max (t ),<br />

<strong>the</strong> dashed line <strong>the</strong> heat sink when ˙q v<br />

∣<br />

∣rm<br />

= ˙q v,min (t ). Despite <strong>the</strong> exemplary<br />

r m -values <strong>of</strong> Figure 4.3, <strong>the</strong>re are two practical approaches to define a reasonable<br />

position for r m,in (and also for r m,ex ). The outcome <strong>of</strong> both is discussed in<br />

Chapter 5.2 regarding NO x emissions. The first approach uses spatially fixed<br />

values for heat introduction and extraction [298], whereas <strong>the</strong> second uses<br />

variable positions [297]. In <strong>the</strong> latter case, <strong>the</strong> positions are coupled with <strong>the</strong><br />

local equivalence ratio φ r . The definition <strong>of</strong> φ r is derived from <strong>the</strong> total equivalence<br />

ratio φ. Since fuel and air diffuse into each o<strong>the</strong>r in <strong>the</strong> area around <strong>the</strong><br />

droplet, <strong>the</strong> ratio <strong>of</strong> nitrogen and oxygen is not constant over <strong>the</strong> radial coordinate<br />

r . Using mass fractions and considering a differential volume enclosing<br />

a differential mass dm, <strong>the</strong> local equivalence ratio φ r can be written as:<br />

φ r =<br />

dm fuel<br />

dm O2<br />

(<br />

mfuel<br />

=<br />

dmY fuel<br />

dmY O2<br />

(<br />

mfuel<br />

=<br />

(<br />

mfuel<br />

Y fuel<br />

Y O2<br />

. (4.42)<br />

m O2<br />

)stoich<br />

m O2<br />

)stoich<br />

m O2<br />

)stoich<br />

Figure 4.4 shows <strong>the</strong> local equivalence ratio φ r in <strong>the</strong> gas phase <strong>of</strong> a single<br />

droplet for different pre-vaporization rates Ψ. <strong>During</strong> vaporization, fuel<br />

(C 10 H 22 ) diffuses away from <strong>the</strong> droplet, whereas oxidizer (O 2 ) diffuses in <strong>the</strong><br />

opposite direction. The local equivalence ratio φ r varies between values ≫ 1<br />

at <strong>the</strong> droplet surface and zero at <strong>the</strong> outer gas phase boundary. Consequently,<br />

<strong>the</strong> spatial position for a constant equivalence ratio also changes for different<br />

pre-vaporization rates Ψ. For low pre-vaporization, this position is close to<br />

<strong>the</strong> droplet surface but shifts far<strong>the</strong>r away from <strong>the</strong> droplet for increasing prevaporization<br />

(given that φ r < 1.5).<br />

4 The absolute time between <strong>the</strong> ignition <strong>of</strong> neighboring droplets τ ign is much longer in <strong>the</strong> work <strong>of</strong> Mikami et al.<br />

[282, 283] and Oyagi et al. [327], as most <strong>of</strong> <strong>the</strong> experiments are conducted with an initial droplet diameter <strong>of</strong><br />

D 0 = 1mm.<br />

133

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