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INAUGURAL–DISSERTATION zur Erlangung der Doktorwürde der ...

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4.1. One-dimensional Evaporating Water Spray in Nitrogen 59<br />

3E+08<br />

Number density [m ­3 ]<br />

2.8E+08<br />

2.6E+08<br />

2.4E+08<br />

2.2E+08<br />

2E+08<br />

1.8E+08<br />

1.6E+08<br />

1.4E+08<br />

1.2E+08<br />

Inhomogeneous<br />

Homogeneous<br />

Experiment<br />

1E+08<br />

8E+07<br />

6E+07<br />

0.14 0.28 0.42 0.56 0.7 0.84<br />

Position [m]<br />

0 1 2 3 4 5<br />

Time [s]<br />

Fig. 4.5: Homogeneous and inhomogeneous calculations of DQMOM.<br />

Before carrying out simulations with an inhomogeneous system of DQMOM transport<br />

Eq. (3.19), homogenous formulations of these equations, given by Eq. (3.20), are<br />

simulated and the results are compared with inhomogeneous computations. Fig. 4.5<br />

shows the computed and experimental profiles of number density at different cross sections<br />

of the spray chamber with homogeneous and inhomogeneous system of DQMOM<br />

equations (see Eq. (3.19)) for 80 kg/h water spray in nitrogen flowing with 0.078 m/s<br />

velocity at 293 K. In the homogeneous results, the time axis of the model is matched<br />

to experimental position through the droplet velocity. The number density decreases<br />

along the spray axis due to droplet evaporation, and the predictions with inhomogeneous<br />

formulation captures the physics of the spray more accurately [198, 200]. Thus,<br />

the present work includes the numerical solutions of the inhomogeneous linear system,<br />

which are formed through application of DQMOM in one physical dimension (axial<br />

direction).<br />

Figure 4.6 displays the results of Sauter mean diameter showing the comparison of<br />

QMOM and DQMOM, where DQMOM results are shown for both lower and higher<br />

Reynolds number. Here, the liquid flow rate is 80 kg/h. It can be seen that the<br />

QMOM results strongly deviate from the experiment whereas DQMOM improves the<br />

results of QMOM significantly even for lower droplet Reynolds numbers, and with<br />

higher Reynolds number, which is the case in this simulations, the agreement between<br />

DQMOM and experiment is very good [191]. A general intuitive question could be<br />

”why the Sauter mean diameter increases in spite of evaporation in simulations as well<br />

as the experiment?”. The answer is elaborated with an example by consi<strong>der</strong>ing the<br />

droplet size distribution of a water spray shown in Fig. 4.7, which displays the droplet

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