Dispersion effectiveness has been tested at various scales, but the comparison of the scales remains a challenge. In the past, researchers have characterized the hydrodynamics in the laboratory scale vessels (ex. baffled flasks) and wave tanks (ex. Ohmsett) to various degrees, however the scalability between systems is a challenge due to the complexity of the apparatus and the disparity in systems. The challenge is to identify the necessary parameters, such as energy dissipation rate and dilution, needed to model dispersion effectiveness across scales.
To accomplish this goal, Computational Fluid Dynamics (CFD) will be used to identify and test dispersion effectiveness parameters and compare modeled results to previous scaled experiments. The purpose of this project is to create a numerical model using dispersant effectiveness data acquired at various scales and under various conditions to correlate effectiveness between systems. These updated models will be used predict dispersion effectiveness at the ocean scale using inputs derived from smaller scale experiments. This work will be done through contract with New Jersey Institute of Technology, with a value of $363,389 and projected end date of June 30, 2026.
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To model DE across scales, Computational Fluid Dynamics (CFD) was used to identify and test the necessary parameters and compare modeled results to previous experiments. Dispersion effectiveness measurements performed in previous studies were used to develop and test the modeling approach. Baffled flask tests were performed with fresh and weathered ANS and Corexit 9500 at dispersant-to-oil ratios of 1:20 and 1:50, along with no dispersant controls. Following completion of the baffled flask test protocol, the droplet size distribution of dispersed oil was measured using a LISST-100x. The VDROP model was used to simulate the conditions in the baffled flasks matching the observed droplets size distribution. Wave tank experiments were performed at Ohmsett using weathered Hibernia. Large-eddy simulation models were used to represent the conditions of plunging breakers and identified the water surface elevation, velocity fields, and vorticity distributions in the Ohmsett tanks. These modeled results were coupled with the VDROP model to predict the droplet size distribution. Modeling the hydrodynamic conditions at both scales was required to understand how to scale data between experimental setups.
Modeling results using VDROP identified the critical variables needed to scale DE. Required inputs to model droplet size distribution, and therefore dispersant effectiveness, are the interfacial tension (based on the dispersant-to-oil ration), oil viscosity, and energy dissipation rates based on ocean conditions. This model allows for more accurate predictions of the droplet size distribution of a target oil in specific sea states. Responders will be able to more accurately predict crude oil transport and dissipation into the water column with and without dispersant applications and ultimately predict the fate of spilled crude oil.