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Simulation results

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4 HPAC model results

4.2 Simulation results

Since HPAC can not take into account deflection of the plume by the momentum of the release jet, the plume is directed along and symmetric about the wind direction as we show in Fig. 4.1. We can therefore not perform a direct comparison of the HPAC results with the experimental data set.

Figure 4.1: HPAC Prediction of the chlorine plume at the end of the 900s release.

We can however do a qualitative comparison, for example of maximum concentrations and plume width.

Chlorine concentration was recorded at several monitor points along four horizontal rows at ground level, located55m,110m,195m,300m,450m, and675mdownwind of the release. The recorded time series were then averaged over the release durationt = 900sand normalized, according to Eq. (3.1), for comparison with the reference data.

4.2.1 Downwind profiles

In Fig. 4.2 we show the computed maximum concentration along the plume both for the two HPAC simulations, with and without topography, and for the experimental data. Note that the HPAC simu-lations appear to show a more rapid dilution of the concentration than observed in the experiments.

In the near field, the distance from the release to the point where the concentration reaches a certain level may vary by a factor of two between the model results and the reference. In the intermediate to far field this distance may be smaller. Note however that the model appears to under-predict in the far field while it is conservative close to the source.

The most important free parameter in the SCIPUFF model used in HPAC is the initial puff parameter σ. As we noted above,σwas chosen to be comparable to the radius of the release jet. In Fig. 4.3 we show the sensitivity of the maximum downwind concentration profile to the choice of this parameter.

Choosing either the radius or the diameter of the jet for the puff parameter result in small differences

Figure 4.2: Maximum concentration along the plume at ground level for HPAC simulations com-pared to the experimental reference data.

in the computed results. Smaller values do however result in much higher near field concentrations and more rapid dilution. The near field concentration is much too high in all these cases. We also tried to vary the lateral puff parameter, σ in order to match the contaminant concentration in the release. In Fig. 4.4 we see that we need to chooseσ > 25mto achieve this. Such a largeσ bears no relation to any physical scale relevant to the release The decay of the maximum concentration profile is still much too rapid, leading to under-prediction at all distances. The resulting plume will also be much too wide because of the large value ofσ.

4.2.2 Cross-wind profiles

In Figs. 4.5–4.10 we show the cross-plume concentration profile at ground level for each of the hor-izontal rows located downstream between55mand675m. We note that the chlorine concentration is larger than the reference values in the near field and smaller than the reference in the far field, in line with the centreline concentration plots shown above. The plume widths predicted with HPAC appear to be significantly larger than the reference data in the near field, whereas plume widths are comparable to the reference data further downstream. As we also observed in the previous section, concentrations levels decay more rapidly in the HPAC simulations.

Most of the observed differences can probably be explained by the lack of a model to account for the momentum-driven jet release. A directed jet release will naturally lead to a narrower plume close to the source, and turbulent entrainment will tend to dilute the near field plume and thus reduce over-prediction.

Figure 4.3: Maximum concentration along the plume at ground level for HPAC simulations com-pared to the experimental reference data. Dependence of theσparameter.

Figure 4.4: Maximum concentration along the plume at ground level for HPAC simulations com-pared to the experimental reference data. Dependence of theσparameter.

Figure 4.5: Cross-plume concentration profile at ground level, 55m downstream of the release.

HPAC simulations compared to the experimental reference data.

Figure 4.6: Cross-plume concentration profile at ground level, 110m downstream of the release.

HPAC simulations compared to the experimental reference data.

Figure 4.7: Cross-plume concentration profile at ground level, 195m downstream of the release.

HPAC simulations compared to the experimental reference data.

Figure 4.8: Cross-plume concentration profile at ground level, 300m downstream of the release.

HPAC simulations compared to the experimental reference data.

Figure 4.9: Cross-plume concentration profile at ground level, 450m downstream of the release.

HPAC simulations compared to the experimental reference data.

Figure 4.10: Cross-plume concentration profile at ground level,675m downstream of the release.

HPAC simulations compared to the experimental reference data.

Figure 5.1: FLUENT and HPAC predictions of the chlorine gas plume at the end of the 900s release.

5 Conclusions

We have compared simulations using CFD techniques (FLUENT) and simple modeling (HPAC) against an experimental data set for the release and dispersion of Chlorine from an industrial facility.

We compare the ground level footprint of the plumes for the two models in Fig. 5.1.

We find that CFD modeling can reproduce the reference data fairly well, both with respect to the trajectory of the plume and to the concentration values. The results do, however, show consistent under-prediction of the plume width and over-prediction of the peak concentration values.

HPAC simulations can not take into account deflection of the plume by the momentum-dominated release jet and plume-building interactions, and thus result in a plume aligned with the wind direc-tion. Dilution of the plume appears to be more rapid in the simulations than in the reference. The plume is much wider in the near field than in the reference; this can in part be explained by the lack of a model to account for the momentum-driven jet release.

References

[1] J. W. Bjerkelund. Analyse av utslipp og spredning av klorgass ved bruk av FLUENT – en vurdering av modelloppbygning og beregning av spredning. MSc thesis, Deptartment of Physics and Technology, University of Bergen., 2007.

[2] J. W. Bjerkelund. Analyse av utslipp og spredning av klorgass ved bruk av FLUENT – en vurdering av modelloppbygning og beregning av spredning. FFI/RAPPORT 2008/00302, Forsvarets Forskningsinstitutt, 2008.

[3] R.I. Sykes, D.S. Henn, S.F. Parker, and R.S. Gabruk. SCIPUFF - a generalized hazard dispersion model. Preprint of the 76th AMS Annual Meeting, Ninth Joint Conference on the Applications of Air Pollution Meteorology with A&WMA, 1996.

[4] R.I. Sykes, C.P. Cerasoli, and D.S. Henn. The representation of dynamic flow effects in a Langrangian puff dispersion model. J. Haz. Mat. A, 64:223–247, 1999.

[5] I.R. Cowan and A.G. Robbins. Project EMU Experimental Data: Case C1. Technical report, EnFlo Research Centre, University of Surrey, 1996.

[6] B. Carissimo, S. F. Jagger, N. C. Daish, A. Halford, S. Selmer-Olsen, K. Riikonen, J.M. Perroux, J. Wurtz, J. Bartzis, N. J. Duim, K. Ham, M. Schatzmann, and R. Hall. The SMEDIS database and validation exercise. Int. J. Environment and Pollution, 16:614–629, 2001.

[7] S.F. Jagger, B. Carissimo, and N. Daish. Definition of parameters for model runs, WP4. Report SMEDIS/96/14/D, SMEDIS Project, October 1998. Draft, Version 0.5.

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