/*---------------------------------------------------------------------------*\ ========= | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox \\ / O peration | \\ / A nd | www.openfoam.com \\/ M anipulation | ------------------------------------------------------------------------------- Copyright (C) 2018 OpenFOAM Foundation ------------------------------------------------------------------------------- License This file is part of OpenFOAM. OpenFOAM is free software: you can redistribute it and/or modify it under the terms of the GNU General Public License as published by the Free Software Foundation, either version 3 of the License, or (at your option) any later version. OpenFOAM is distributed in the hope that it will be useful, but WITHOUT ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License for more details. You should have received a copy of the GNU General Public License along with OpenFOAM. If not, see . Class Foam::diameterModels::daughterSizeDistributionModels:: LaakkonenAlopaeusAittamaaDsd Description Daughter size distribution model used by Laakkonen et al. (2006). Note that it must be multiplied by the number of daughter particles (2). Also, the coefficient C4 needs to be set to the value of 2 as to ensure number and mass conservation following Kumar and Ramkrishna (1996). Also the internal coordinate was changed to particle volume, which gives \f[ \frac{60}{v_j} \left(\frac{v_i}{v_j}\right)^{2} \left(1 - \frac{v_i}{v_j}\right)^{2} \f] where \vartable v_i | Volume of daughter bubble i [m] v_j | Volume of mother bubble j [m] \endvartable References: \verbatim Laakkonen, M., Alopaeus, V., & Aittamaa, J. (2006). Validation of bubble breakage, coalescence and mass transfer models for gas-liquid dispersion in agitated vessel. Chemical engineering science, 61(1), 218-228. Eq. 3, p. 220. \endverbatim \verbatim Kumar, S., & Ramkrishna, D. (1996). On the solution of population balance equations by discretization-I. A fixed pivot technique. Chemical Engineering Science, 51(8), 1311-1332. Eq. 33, p. 1318. \endverbatim Usage \table Property | Description | Required | Default value C1 | Coefficient C1 | no | 6.0 C2 | Coefficient C2 | no | 0.04 C3 | Coefficient C3 | no | 0.01 \endtable SourceFiles LaakkonenAlopaeusAittamaaBinaryBreakup.C \*---------------------------------------------------------------------------*/ #ifndef LaakkonenAlopaeusAittamaaDsd_H #define LaakkonenAlopaeusAittamaaDsd_H #include "daughterSizeDistributionModel.H" // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // namespace Foam { namespace diameterModels { namespace daughterSizeDistributionModels { /*---------------------------------------------------------------------------*\ Class LaakkonenAlopaeusAittamaaDsd Declaration \*---------------------------------------------------------------------------*/ class LaakkonenAlopaeusAittamaaDsd : public daughterSizeDistributionModel { public: //- Runtime type information TypeName("LaakkonenAlopaeusAittamaa"); // Constructor LaakkonenAlopaeusAittamaaDsd ( const breakupModel& breakup, const dictionary& dict ); //- Destructor virtual ~LaakkonenAlopaeusAittamaaDsd(); // Member Functions //- Return total number of particles assigned to class i when a particle // of class k breaks virtual dimensionedScalar calcNik(const label i, const label k) const; }; // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // } // End namespace daughterSizeDistributionModels } // End namespace diameterModels } // End namespace Foam // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // #endif // ************************************************************************* //