Loading README.md +1 −1 Original line number Diff line number Diff line Loading @@ -31,7 +31,7 @@ can be built locally by: 1. Install sphinx: ```shell > pip install sphinx sphinx_rtd_theme sphinx-tabs > pip install sphinx sphinx_rtd_theme sphinx-tabs sphinxcontrib-bibtex ``` 2. Build the documentation: Loading docs/source_docs/refs.bib +61 −0 Original line number Diff line number Diff line Loading @@ -82,6 +82,15 @@ pages = {379-402} url = {https://www.sciencedirect.com/science/article/pii/S0021999120305945}, } @article{brinkman52, author = {Brinkman, H.C.}, title = {The viscosity of concentrated suspensions and solutions}, journal = {The Journal of Chemical Physics}, year = {1952}, volume = {20}, pages = {571} } @book{Burden10, title={Numerical Analysis}, author={Burden, R.L. and Faires, J.D.}, Loading @@ -101,6 +110,14 @@ pages = {379-402} pages = {1-31} } @article{cheng03, author = {Nian-Sheng Cheng and Adrian Wing-Keung Law}, title = {Exponential formula for computing effective viscosity}, journal = {Powder Technology}, year = {2003}, volume = {129}, pages = {156--160} } @techreport{chern87, author = {Chern, I.-L., and Colella, P. }, Loading Loading @@ -190,6 +207,15 @@ pages = {379-402} publisher={Oxford University Computing Laboratory Oxford, UK} } @article{einstein11, title={Eine neue bestimmung der moleküldimensionen}, author={Einstein, A}, journal={Ann. Physik}, volume={19}, pages={289--306}, year={1911}, } @article{elhilo12, author = {M. El-Hilo and R.W. Chantrell}, title = {Rationalisation of distribution functions for models of nanoparticle magnetism}, Loading Loading @@ -238,6 +264,15 @@ url = {https://www.sciencedirect.com/science/article/pii/S0304885312002132}, publisher={Elsevier} } @article{gibilaro07, author = {Gibilaro L.G., Gallucci K., Felice R. Di. and Pagliai P.}, title = {On the apparent viscosity of a fluidized bed}, journal = {Chemical Engineering Science}, year = {2007}, volume = {62}, pages = {294--300} } @article{Gid83, author = {Gidaspow, D. and Ettehadieh, B. }, title = {Fluidization in Two-Dimensional Beds with a Jet; 2. Hydrodynamic Modeling}, Loading Loading @@ -290,6 +325,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, pages = {843-855} } @article{krieger59, author = {Krieger, I.M. and Dougherty, T.J. }, title = {A mechanism for non-newtonian flow in suspensions of rigid spheres}, journal = {Trans. Soc. Rheol}, year = {1959}, volume = {3}, pages = {137--152} } @article{Lat011, author = {Lathouwers, D. and Bellan, J. }, title = {Modeling of dense gas-solid reative mixtures applied to biomass pyrolysis in a fluidized bed}, Loading Loading @@ -330,6 +374,14 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, publisher = {NOAA/NCAR Boulder Atmospheric Observatory}, } @article{maron56, author = {Samuel H Maron and Percy E Pierce}, title = {Application of ree-eyring generalized flow theory to suspensions of spherical particles}, journal = {Journal of Colloid Science}, year = {1956}, volume = {11}, pages = {80--95} } @article{Massoudi03, author = {Mehrdad Massoudi}, Loading Loading @@ -384,6 +436,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, volume = {32} } @article{roscoe52, author = {Roscoe, R.}, title = {The viscosity of suspensions of rigid spheres}, journal = {British Journal of Applied Physics}, year = {1952}, volume = {3}, pages = {267} } @article{Sch33, author = {Schiller, L. and Naumann, A. }, title = {A drag coefficient correlation}, Loading docs/source_docs/user_guide/inputs/fluid_model.rst +38 −1 Original line number Diff line number Diff line Loading @@ -35,10 +35,47 @@ The following inputs are defined using the ``fluid`` prefix. | viscosity.eddy.Smagorinsky-Lilly.constant | Smagorinsky-Lilly constant which usually has values | Real | None | | | between 0.1 and 0.2. | | | | | | | | | | A value is required when using the ``Samgorinsky-Lilly`` | | | | | A value is required when using the ``Smagorinsky-Lilly`` | | | | | eddy viscosity model. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.eddy.WALE.constant | WALE eddy viscosity model constant. | Real | 0.325 | ---------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension | Specify suspension viscosty model of the form | String | None | | | :math:`\mu_{susp}=\mu_{mol}(\mu^* - 1)` | | | | | | | | | | Available options include: | | | | | | | | | | * ``None`` No eddy suspension model | | | | | :math:`\mu^*=1` | | | | | | | | | | * ``Einstein`` :cite:p:`einstein11` | | | | | :math:`\mu^*=1 + 2.5\varepsilon_s` | | | | | | | | | | * ``Brinkman`` :cite:p:`brinkman52,gibilaro07` | | | | | :math:`\mu^*=(1-\varepsilon_s)^{-c}` | | | | | | | | | | * ``Roscoe`` :cite:p:`roscoe52,krieger59,maron56` | | | | | :math:`\mu^*=(1-\varepsilon_s/c_1)^{-c_2}` | | | | | | | | | | * ``ChengLaw`` :cite:p:`cheng03` | | | | | :math:`\mu^*=e^{2.5(1/(1-\varepsilon_s)^c-1)/c}` | | | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Brinkman.constant | Constant for exponent in Brinkman suspension expression. | Real | None | | | | | | | | A value is required when using the model ``Brinkman``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Roscoe.c1 | Constant for max packing in Roscoe suspension expression. | Real | None | | | | | | | | A value is required when using the model ``Roscoe``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Roscoe.c2 | Constant for exponent in Roscoe suspension expression. | Real | None | | | | | | | | A value is required when using the model ``Roscoe``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.ChengLaw.constant | Constant for exponent in ChengLaw suspension expression. | Real | None | | | | | | | | A value is required when using the model ``ChengLaw``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | species | Specify the species that constitute the fluid. | String | None | | | | | | Loading Loading
README.md +1 −1 Original line number Diff line number Diff line Loading @@ -31,7 +31,7 @@ can be built locally by: 1. Install sphinx: ```shell > pip install sphinx sphinx_rtd_theme sphinx-tabs > pip install sphinx sphinx_rtd_theme sphinx-tabs sphinxcontrib-bibtex ``` 2. Build the documentation: Loading
docs/source_docs/refs.bib +61 −0 Original line number Diff line number Diff line Loading @@ -82,6 +82,15 @@ pages = {379-402} url = {https://www.sciencedirect.com/science/article/pii/S0021999120305945}, } @article{brinkman52, author = {Brinkman, H.C.}, title = {The viscosity of concentrated suspensions and solutions}, journal = {The Journal of Chemical Physics}, year = {1952}, volume = {20}, pages = {571} } @book{Burden10, title={Numerical Analysis}, author={Burden, R.L. and Faires, J.D.}, Loading @@ -101,6 +110,14 @@ pages = {379-402} pages = {1-31} } @article{cheng03, author = {Nian-Sheng Cheng and Adrian Wing-Keung Law}, title = {Exponential formula for computing effective viscosity}, journal = {Powder Technology}, year = {2003}, volume = {129}, pages = {156--160} } @techreport{chern87, author = {Chern, I.-L., and Colella, P. }, Loading Loading @@ -190,6 +207,15 @@ pages = {379-402} publisher={Oxford University Computing Laboratory Oxford, UK} } @article{einstein11, title={Eine neue bestimmung der moleküldimensionen}, author={Einstein, A}, journal={Ann. Physik}, volume={19}, pages={289--306}, year={1911}, } @article{elhilo12, author = {M. El-Hilo and R.W. Chantrell}, title = {Rationalisation of distribution functions for models of nanoparticle magnetism}, Loading Loading @@ -238,6 +264,15 @@ url = {https://www.sciencedirect.com/science/article/pii/S0304885312002132}, publisher={Elsevier} } @article{gibilaro07, author = {Gibilaro L.G., Gallucci K., Felice R. Di. and Pagliai P.}, title = {On the apparent viscosity of a fluidized bed}, journal = {Chemical Engineering Science}, year = {2007}, volume = {62}, pages = {294--300} } @article{Gid83, author = {Gidaspow, D. and Ettehadieh, B. }, title = {Fluidization in Two-Dimensional Beds with a Jet; 2. Hydrodynamic Modeling}, Loading Loading @@ -290,6 +325,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, pages = {843-855} } @article{krieger59, author = {Krieger, I.M. and Dougherty, T.J. }, title = {A mechanism for non-newtonian flow in suspensions of rigid spheres}, journal = {Trans. Soc. Rheol}, year = {1959}, volume = {3}, pages = {137--152} } @article{Lat011, author = {Lathouwers, D. and Bellan, J. }, title = {Modeling of dense gas-solid reative mixtures applied to biomass pyrolysis in a fluidized bed}, Loading Loading @@ -330,6 +374,14 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, publisher = {NOAA/NCAR Boulder Atmospheric Observatory}, } @article{maron56, author = {Samuel H Maron and Percy E Pierce}, title = {Application of ree-eyring generalized flow theory to suspensions of spherical particles}, journal = {Journal of Colloid Science}, year = {1956}, volume = {11}, pages = {80--95} } @article{Massoudi03, author = {Mehrdad Massoudi}, Loading Loading @@ -384,6 +436,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, volume = {32} } @article{roscoe52, author = {Roscoe, R.}, title = {The viscosity of suspensions of rigid spheres}, journal = {British Journal of Applied Physics}, year = {1952}, volume = {3}, pages = {267} } @article{Sch33, author = {Schiller, L. and Naumann, A. }, title = {A drag coefficient correlation}, Loading
docs/source_docs/user_guide/inputs/fluid_model.rst +38 −1 Original line number Diff line number Diff line Loading @@ -35,10 +35,47 @@ The following inputs are defined using the ``fluid`` prefix. | viscosity.eddy.Smagorinsky-Lilly.constant | Smagorinsky-Lilly constant which usually has values | Real | None | | | between 0.1 and 0.2. | | | | | | | | | | A value is required when using the ``Samgorinsky-Lilly`` | | | | | A value is required when using the ``Smagorinsky-Lilly`` | | | | | eddy viscosity model. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.eddy.WALE.constant | WALE eddy viscosity model constant. | Real | 0.325 | ---------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension | Specify suspension viscosty model of the form | String | None | | | :math:`\mu_{susp}=\mu_{mol}(\mu^* - 1)` | | | | | | | | | | Available options include: | | | | | | | | | | * ``None`` No eddy suspension model | | | | | :math:`\mu^*=1` | | | | | | | | | | * ``Einstein`` :cite:p:`einstein11` | | | | | :math:`\mu^*=1 + 2.5\varepsilon_s` | | | | | | | | | | * ``Brinkman`` :cite:p:`brinkman52,gibilaro07` | | | | | :math:`\mu^*=(1-\varepsilon_s)^{-c}` | | | | | | | | | | * ``Roscoe`` :cite:p:`roscoe52,krieger59,maron56` | | | | | :math:`\mu^*=(1-\varepsilon_s/c_1)^{-c_2}` | | | | | | | | | | * ``ChengLaw`` :cite:p:`cheng03` | | | | | :math:`\mu^*=e^{2.5(1/(1-\varepsilon_s)^c-1)/c}` | | | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Brinkman.constant | Constant for exponent in Brinkman suspension expression. | Real | None | | | | | | | | A value is required when using the model ``Brinkman``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Roscoe.c1 | Constant for max packing in Roscoe suspension expression. | Real | None | | | | | | | | A value is required when using the model ``Roscoe``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Roscoe.c2 | Constant for exponent in Roscoe suspension expression. | Real | None | | | | | | | | A value is required when using the model ``Roscoe``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.ChengLaw.constant | Constant for exponent in ChengLaw suspension expression. | Real | None | | | | | | | | A value is required when using the model ``ChengLaw``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | species | Specify the species that constitute the fluid. | String | None | | | | | | Loading
