- Available solvers with hybrid approximation
- Meeting points for users and developers
- Available OpenFOAM versions
- Derived projects
- Research studies where the library was useful
- For citation
United collection of hybrid Central solvers based on central-upwind schemes of Kurganov and Tadmor and LTS support for steady-state calculations: one-phase, two-phase and multicomponent versions.
Only OpenFOAM+ version of the OpenFOAM technology is supported since 2018. The framework contains next solvers:
- Compressible single phase flow solvers:
- pimpleCentralFoam - Pressure-based semi implicit solver for compressible flow of perfect gas
- rhoPimpleCentralFoam - Pressure-based semi implicit solver for compressible flow of real gas
- pimpleCentralDyMFoam - Pressure-based semi implicit solver for compressible flow of perfect gas with mesh motion and AMR
- chtMultiRegionCentralFoam - Pressure-based semi implicit solver for conjugate simulation of compressible perfect gas flow (Mach number is ranging from 0 to 6) and solid body heat transfer.
- Multi-component solvers:
- reactingPimpleCentralFoam - Pressure-based semi implicit solver for compressible flow with combustion and chemical reactions
- reactingLagrangianPimpleCentralFoam - Pressure-based semi implicit solver for compressible flow with combustion, particles motion, phase change and chemical reactions
- Multi-phase solvers:
- vofTwoPhaseCentralFoam - an improved version (since OpenFOAM+ 2312) of interTwoPhaseCentralFoam solver that uses volumetric fluxes for transport (increased robustness).
- interTwoPhaseCentralFoam - pressure-based solver for compressible (0-4 Mach numbers) flow of two-phase media with account to viscosity and gravity. The solver utilizes VoF method for resolution of phase interface and ACID technique ( https://doi.org/10.1016/j.jcp.2018.04.028) to calculate properties in the region where both phases are present.
- twoPhaseMixingCentralFoam - Transient Eulerian two-phase solver. Liquid and gas are considered as compressible fluids. Mass transfer at the interface is not accounted.
- twoPhaseMixingCentralDyMFoam - Transient Eulerian two-phase solver with dynamic meshes. Liquid and gas are considered as compressible fluids. Mass transfer at the interface is not accounted.
You can discuss questions of hybridCentralSolvers usage at Telegram Group: https://t.me/hybridCentralSolvers
There is a ResearchGate project dedicated to the development of hybridCentralSolvers library
The library is available for next versions of OpenFOAM:
- OpenFOAM 3.1 - master branch
- OpenFOAM 4.1 - dev-of4.1 branch
- OpenFOAM 6 - dev-of6 branch
- OpenFOAM+ 1812 - digitef-dev-1812
- OpenFOAM+ 1912 - digitef-dev-1912
- OpenFOAM+ 2012 - digitef-dev-2012
- OpenFOAM+ 2112 - digitef-dev-2112
- OpenFOAM+ 2212 - digitef-dev-2212
- OpenFOAM+ 2312 - digitef-dev-2312
Latest changes and bug fixes are applied only in branches corresponding to latest version of OpenFOAM.
The library or approach were used in next projects:
- multiRegionRectingPimpleCentralFoam - the solver for coupled simulation of gas dynamics and heat transfer using hybrid KT/PIMPLE approximation of convective fluxes
- adjointReactingRhoPimpleCentralFoam - the solver for adjoint shape optimization of region with gas flow modelled using hybrid KT/PIMPLE approximation of convective fluxes
If you want to see your research in this list, please write to Issues .
When using these solvers, please cite the following works:
- Kraposhin MV, Banholzer M, Pfitzner M, Marchevsky IK. A hybrid pressure‐based solver for nonideal single‐phase fluid flows at all speeds. Int J Numer Meth Fluids. 2018;88:79–99. https://doi.org/10.1002/fld.4512
- Kraposhin MV, Strijhak SV, Bovtrikova A Adaptation of Kurganov-Tadmor Numerical Scheme for Applying in Combination with the PISO Method in Numerical Simulation of Flows in a Wide Range of Mach Numbers. Procedia Computer Science. 2015;66:43-52. https://doi.org/10.1016/j.procs.2015.11.007
- Kraposhin, M., Kukharskii, A., Victoria, & Shevelev, A. (2022). An extension of the all-Mach number pressure-based solution framework for numerical modelling of two-phase flows with interface. Industrial Processes and Technologies, 2(3(5), 6–27. https://doi.org/10.37816/2713-0789-2022-2-3(5)-6-27