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

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5 Results<br />

uses constant spatial positions for heat introduction and extraction. It is <strong>the</strong><br />

basis for <strong>the</strong> results <strong>of</strong> Chapter 5.2.1. The second approach enforces ignition<br />

at a position r m,in <strong>of</strong> constant local equivalence ratio φ r (cf. Eq. (4.42)). Here,<br />

<strong>the</strong> effective local equivalence ratio is fixed to φ r = 0.5. The advantage is to<br />

ensure a safe ignition for all degrees <strong>of</strong> vaporization Ψ without receiving overlapping<br />

volumes <strong>of</strong> droplet and heat source, which can become crucial particularly<br />

at low values <strong>of</strong> Ψ. Since <strong>the</strong> heat source is distributed over a finite<br />

volume around r m,in , heat is also introduced at positions where φ r > 0.5. This<br />

ensures a safe ignition. The results <strong>of</strong> this second approach are discussed in<br />

<strong>the</strong> present chapter and compared with <strong>the</strong> previous results <strong>of</strong> Chapter 5.2.1.<br />

For <strong>the</strong> heat extraction following a successful ignition, two different cases are<br />

considered: In <strong>the</strong> first case, a spatially fixed position <strong>of</strong> <strong>the</strong> heat extraction<br />

(i.e. <strong>the</strong> heat sink in Fig. 5.4) <strong>of</strong> r m,ex = 1.4×10 −3 m is used in combination with<br />

all ignition positions r m,in (i.e. <strong>the</strong> heat source in Fig. 5.4). This case <strong>of</strong> heat<br />

extraction is termed “heat sink at fixed position”. In <strong>the</strong> second case, <strong>the</strong> position<br />

<strong>of</strong> <strong>the</strong> heat extraction r m,ex is coupled to <strong>the</strong> (variable) ignition position<br />

r m,in by <strong>the</strong> fixed distance <strong>of</strong> 0.6×10 −3 m. This latter case <strong>of</strong> heat extraction is<br />

termed “heat sink at fixed distance” [297].<br />

Differences <strong>of</strong> <strong>the</strong> Approaches Applied for Ignition Modeling<br />

The resulting mean positions <strong>of</strong> heat introduction, r m,in , and heat extraction,<br />

r m,ex , are depicted in Figure 5.4 as a function <strong>of</strong> pre-vaporization rate<br />

Ψ. The positions <strong>of</strong> r m,in are marked with squares for heat sources, whereas<br />

<strong>the</strong> positions <strong>of</strong> r m,ex are marked with circles for heat sinks. As introduced<br />

in Chapter 4.3 and Figure 4.3, <strong>the</strong> expansion <strong>of</strong> <strong>the</strong> respective volumes V in/ex<br />

(Eq. (4.36)) is indicated in Figure 5.4 by vertical bars, ranging from r min<br />

(Eq. (4.37)) to r max (Eq. (4.38)). Even though <strong>the</strong>se limiting minimum and<br />

maximum positions vary with Ψ, depending on <strong>the</strong> mean positions r m,in/ex ,<br />

<strong>the</strong> effective volumes <strong>of</strong> heat introduction and extraction are <strong>of</strong> constant size.<br />

Starting from a low pre-vaporization rate <strong>of</strong> Ψ= 0.15, Figure 5.4 unveils a shift<br />

<strong>of</strong> <strong>the</strong> ignition position away from <strong>the</strong> droplet until a maximum is reached<br />

around Ψ= 0.7. Fur<strong>the</strong>rmore, an overlap can be identified between heat introduction<br />

and extraction volume in <strong>the</strong> range <strong>of</strong> Ψ= 0.15 to 0.4. For comparison,<br />

<strong>the</strong> fixed positions as employed in Chapter 5.2.1 are shown on <strong>the</strong> right<br />

hand side <strong>of</strong> Figure 5.4.<br />

164

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