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

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3 Experiments on Droplet Array <strong>Combustion</strong><br />

W m −1 K −1 . All <strong>the</strong>se property values refer to <strong>the</strong> gaseous state, as liquid fuel is<br />

not part <strong>of</strong> this CFD simulation.<br />

Figure 3.22 illustrates <strong>the</strong> temporal evolution <strong>of</strong> <strong>the</strong> combustion process during<br />

<strong>the</strong> initial second, starting from ignition. Left and right side <strong>of</strong> <strong>the</strong> figure<br />

depict <strong>the</strong> vertical middle plane <strong>of</strong> <strong>the</strong> combustion chamber with z = 0mm<br />

(cf. Fig. 3.7). The left side shows <strong>the</strong> temperature pr<strong>of</strong>ile in <strong>the</strong> gaseous phase<br />

with <strong>the</strong> five fuel sources being <strong>the</strong> locations <strong>of</strong> <strong>the</strong> lowest temperatures,<br />

whereas <strong>the</strong> right side shows <strong>the</strong> velocity field indicated by <strong>the</strong> absolute velocity|v|=(vx<br />

2+ v 2 y + v z 2) 2 1 . The velocity vector <strong>of</strong> <strong>the</strong> flow is visualized by white<br />

streamlines. Being <strong>the</strong> main subject <strong>of</strong> this first part <strong>of</strong> <strong>the</strong> CFD study, <strong>the</strong><br />

discharge <strong>of</strong> hot exhaust gas from <strong>the</strong> open bottom <strong>of</strong> <strong>the</strong> combustion chamber<br />

by convection is clearly indicated by <strong>the</strong> evolution <strong>of</strong> <strong>the</strong> temperature and<br />

velocity fields. This process is particularly responsible for <strong>the</strong> temperature<br />

field becoming more and more asymmetric along <strong>the</strong> axis <strong>of</strong> <strong>the</strong> droplet array.<br />

Here, <strong>the</strong> initial time (t = 0s) is defined as <strong>the</strong> time when ignition is enforced<br />

by <strong>the</strong> implemented heat release mechanism. Ignition <strong>of</strong> <strong>the</strong> first droplet occurs<br />

at t = 29 ms with a local temperature rise to 2118 K. Starting from this<br />

local kernel, <strong>the</strong> flame front propagates along <strong>the</strong> flammable gas layer, forming<br />

a spherical flame around <strong>the</strong> fuel source. At t = 0.2 s, <strong>the</strong> flame ball around<br />

<strong>the</strong> first fuel source is fully developed and a temperature <strong>of</strong> T = T max = 2515 K<br />

is indicated. Subsequently, <strong>the</strong> flame spreads from fuel source to fuel source<br />

(Fig. 3.22, from left to right). At t = 0.4s, <strong>the</strong> fourth droplet is ignited but not<br />

yet enclosed by <strong>the</strong> flame. The ensuing flame propagation and volume expansion<br />

due to combustion are clearly observable in combination with <strong>the</strong> contour<br />

plot <strong>of</strong> absolute velocity |v|. At t = 0.6s, all fuel sources are ignited and<br />

<strong>the</strong> flame stabilizes at a high burning rate k. Still, a small eddy <strong>of</strong> unburned<br />

air prevails in <strong>the</strong> upper right corner <strong>of</strong> <strong>the</strong> droplet array holder before it dissipates<br />

around t = 0.8 s. It is a consequence <strong>of</strong> flame propagation towards <strong>the</strong><br />

“cold, metallic containment” <strong>of</strong> <strong>the</strong> droplet array holder. Finally, <strong>the</strong> highest<br />

velocities within <strong>the</strong> combustion chamber are observed at <strong>the</strong> opening in <strong>the</strong><br />

vicinity <strong>of</strong> <strong>the</strong> vertical props with|v| max = 0.595 m s −1 at t = 0.6s. After ignition<br />

<strong>of</strong> <strong>the</strong> fourth and fifth fuel source, <strong>the</strong> flow field becomes uniform, as underlined<br />

by <strong>the</strong> white streamlines.<br />

The utilized single-step mechanism <strong>of</strong> Westbrook and Dryer [459] can inherently<br />

only be an approximation, as it is trimmed mainly to predict correct<br />

flame speeds S L . Thus, it is subject to some restrictions: At flame temperatures<br />

108

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