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

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4 Numerical Modeling and Simulation<br />

1.50<br />

1.40<br />

Experiments (Xu et al., 2003)<br />

Simulation<br />

mm s −1 Initial droplet diameter D 0<br />

Burning rate k<br />

1.30<br />

1.20<br />

1.10<br />

1.00<br />

0.8 1.0 1.2 1.4 1.6 mm<br />

Experi-<br />

Figure 4.10: Evaluation <strong>of</strong> Burning Rate for Different Initial Droplet Diameters.<br />

ments and numerical simulations were conducted at T ∞ = 1093K [465].<br />

to <strong>the</strong> fact that <strong>the</strong> effects <strong>of</strong> radiation and soot formation, as for instance reported<br />

in Nakaya et al. [307, 309] and Xu et al. [465, 467], are not taken into<br />

account in <strong>the</strong> present single droplet model. Besides, this particular validation<br />

test case at T ∞ = 1093 K yields <strong>the</strong> same k-value for droplets burning due<br />

to auto-ignition as well as due to forced ignition by an external heat source<br />

(cf. Chap. 4.3). However, auto-ignition requires more ignition delay time than<br />

forced ignition.<br />

4.7 Scope and Limitations <strong>of</strong> Single Droplet <strong>Combustion</strong><br />

Utilizing <strong>the</strong> one-dimensional single droplet model, as outlined above (see<br />

Chap. 4.5), it is not possible to investigate two or more droplets including<br />

<strong>the</strong>ir interactions. Effects <strong>of</strong> convective flow cannot be studied ei<strong>the</strong>r. <strong>On</strong> <strong>the</strong><br />

o<strong>the</strong>r hand, detailed chemistry modeling, as required within this study, necessitates<br />

massive computational resources. The computation <strong>of</strong> a full geometry<br />

comparable to <strong>the</strong> one <strong>of</strong> Chapter 3.3 with detailed chemistry is infeasible at<br />

present and will remain to be so for <strong>the</strong> foreseeable future. However, it may<br />

150

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