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Commit 46f2be6d authored by Deepak Rangarajan's avatar Deepak Rangarajan Committed by Jordan Musser
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Add Sato option from MR 1429 (!113)

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1 merge request!113Add Sato option from MR 1429
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...@@ -464,6 +464,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, ...@@ -464,6 +464,15 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305},
pages = {267} 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, @article{Sch33,
author = {Schiller, L. and Naumann, A. }, author = {Schiller, L. and Naumann, A. },
title = {A drag coefficient correlation}, title = {A drag coefficient correlation},
......
...@@ -21,6 +21,8 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill ...@@ -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)}` .. |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 | | | Description | Type | Default |
+============================================+============================================================+========+==========+ +============================================+============================================================+========+==========+
...@@ -104,6 +106,10 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill ...@@ -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}` | | | | | :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 | | viscosity.suspension.Brinkman.constant | Constant for exponent in Brinkman suspension expression. | Real | None |
| | | | | | | | | |
...@@ -121,6 +127,9 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill ...@@ -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``. | | | | | 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 | | viscosity.max_effective_factor | Max limit of the effective viscosity as a factor of the | Real | 1.e6 |
| | molecular viscosity | | | | | molecular viscosity | | |
| | | | | | | | | |
......
...@@ -56,8 +56,6 @@ The following inputs must be preceded by "mfix." and control what variables will ...@@ -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 | 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_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 | | plt_volfrac | Save Eulerian grid volume fraction (from cut cells) to plot file | Int | 0 |
......
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