Loading docs/source_docs/refs.bib +9 −0 Original line number Diff line number Diff line Loading @@ -464,6 +464,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, pages = {267} } @article{sato81, author = {Sato, Y. and Sadatomi, M.}, title = {Momentum and heat transfer in two-phase bubble flow - I. Theory}, journal = {International Journal of Multiphase Flow}, year = {1981}, volume = {7}, pages = {167-177} } @article{Sch33, author = {Schiller, L. and Naumann, A. }, title = {A drag coefficient correlation}, Loading docs/source_docs/user_guide/inputs/fluid_model.rst +9 −0 Original line number Diff line number Diff line Loading @@ -21,6 +21,8 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill .. |Reid_4parm_Eq| replace:: :math:`\mu(T) = A\exp{\left( \frac{B}{T} + CT + DT^2 \right)}` .. |Sato_Eq| replace:: :math:`\mu^* = 1 + C d_s \rho \mu_{mol} \left|\boldsymbol{u} - \boldsymbol{u_s}\right|` +--------------------------------------------+------------------------------------------------------------+--------+----------+ | | Description | Type | Default | +============================================+============================================================+========+==========+ Loading Loading @@ -104,6 +106,10 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill | | | | | | | :math:`\mu^*=e^{2.5(1/(1-\varepsilon_s)^c-1)/c}` | | | | | | | | | | * ``Sato`` :cite:p:`sato81` | | | | | | | | | | |Sato_Eq| | | | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Brinkman.constant | Constant for exponent in Brinkman suspension expression. | Real | None | | | | | | Loading @@ -121,6 +127,9 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill | | | | | | | A value is required when using the model ``ChengLaw``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Sato.constant | Constant for Sato suspension expression. | Real | 0.65 | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.max_effective_factor | Max limit of the effective viscosity as a factor of the | Real | 1.e6 | | | molecular viscosity | | | | | | | | Loading docs/source_docs/user_guide/inputs/output/plotfiles.rst +0 −2 Original line number Diff line number Diff line Loading @@ -56,8 +56,6 @@ The following inputs must be preceded by "mfix." and control what variables will +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_mu_g | Save fluid molecular viscosity to plot file | Int | 0 | +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_mu_g_eff | Save fluid effective viscosity to plot file | Int | 0 | +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_diveu | Save div(ep_g . u) to plot file | Int | 0 | +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_volfrac | Save Eulerian grid volume fraction (from cut cells) to plot file | Int | 0 | Loading Loading
docs/source_docs/refs.bib +9 −0 Original line number Diff line number Diff line Loading @@ -464,6 +464,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, pages = {267} } @article{sato81, author = {Sato, Y. and Sadatomi, M.}, title = {Momentum and heat transfer in two-phase bubble flow - I. Theory}, journal = {International Journal of Multiphase Flow}, year = {1981}, volume = {7}, pages = {167-177} } @article{Sch33, author = {Schiller, L. and Naumann, A. }, title = {A drag coefficient correlation}, Loading
docs/source_docs/user_guide/inputs/fluid_model.rst +9 −0 Original line number Diff line number Diff line Loading @@ -21,6 +21,8 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill .. |Reid_4parm_Eq| replace:: :math:`\mu(T) = A\exp{\left( \frac{B}{T} + CT + DT^2 \right)}` .. |Sato_Eq| replace:: :math:`\mu^* = 1 + C d_s \rho \mu_{mol} \left|\boldsymbol{u} - \boldsymbol{u_s}\right|` +--------------------------------------------+------------------------------------------------------------+--------+----------+ | | Description | Type | Default | +============================================+============================================================+========+==========+ Loading Loading @@ -104,6 +106,10 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill | | | | | | | :math:`\mu^*=e^{2.5(1/(1-\varepsilon_s)^c-1)/c}` | | | | | | | | | | * ``Sato`` :cite:p:`sato81` | | | | | | | | | | |Sato_Eq| | | | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Brinkman.constant | Constant for exponent in Brinkman suspension expression. | Real | None | | | | | | Loading @@ -121,6 +127,9 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill | | | | | | | A value is required when using the model ``ChengLaw``. | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Sato.constant | Constant for Sato suspension expression. | Real | 0.65 | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.max_effective_factor | Max limit of the effective viscosity as a factor of the | Real | 1.e6 | | | molecular viscosity | | | | | | | | Loading
docs/source_docs/user_guide/inputs/output/plotfiles.rst +0 −2 Original line number Diff line number Diff line Loading @@ -56,8 +56,6 @@ The following inputs must be preceded by "mfix." and control what variables will +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_mu_g | Save fluid molecular viscosity to plot file | Int | 0 | +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_mu_g_eff | Save fluid effective viscosity to plot file | Int | 0 | +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_diveu | Save div(ep_g . u) to plot file | Int | 0 | +---------------------+-----------------------------------------------------------------------+-------------+-----------+ | plt_volfrac | Save Eulerian grid volume fraction (from cut cells) to plot file | Int | 0 | Loading
