Tor Harald Sandve
fd219dd544
Add whitespaces and comments to beautify the code
2016-02-17 10:43:01 +01:00
Tor Harald Sandve
b02589316f
Add support for MISC regions
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- element wise power operator impemented in AutoDiffBlock
- TL parameters are given pr cell
2016-02-15 14:44:14 +01:00
Tor Harald Sandve
0a30d912e8
Some more cleanup adressing PR comments.
2016-02-12 11:02:03 +01:00
Tor Harald Sandve
dee96db6b2
Cleaning and adding comments
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
0745be3eba
Various bugfixes in computing effective ToddLongstaff parameters
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The most significant bug was in the computation of effective saturation
fraction for the gas phase. The current implementation differs from the
manual.
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
a38964c641
Some cleaning
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
13117153a9
Use effective properties in the computation of well segment densities
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
beafccc038
Refactor the ToddLongstaffModel in separate function
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
b8e20917cc
Add Todd and Longstaff model
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Add method to calculateEffectiveProperties (viscosity and density)
using the Todd and Longstaff model.
The effective properties are stored in mu_eff_ and b_eff_ in the
BlackoilSolventModel and accessed using fluidReciprocFVF and
fluidViscosity
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
38c8cd981e
BUGFIX. Fix surfaceDensity calculations
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
1e64409f28
Scaling of relative permeability endpoints by the miscibility function
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
bcb0abd9c9
Fix well input and prepare for critical saturations
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
e448548d5a
Some refactoring to avoid code duplication
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computeMassFlux in BlackoilSolventModel_impl.hpp is refactored to avoid
code duplication
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
238e7c19f3
Add support for miscibilty in the relperms
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
bbee43ef7a
Refactor computeMassFlux in the SolventModel
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The computeMassFlux in the solventModel is refactored to allow for
modification of relperms for all phases.
2016-02-12 10:42:26 +01:00
Tor Harald Sandve
a47c9add9b
Change interface of surfaceDensity()
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Add phaseIdx as input and return array of n density values for the
phase. And adapt the usage accordingly.
2015-11-10 14:54:49 +01:00
Tor Harald Sandve
a46b64adcd
Support for non constant surface densities
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The surface density function returns one value pr cell to allow for non
constant surface densities.
2015-11-10 12:49:19 +01:00
Markus Blatt
6ee021f0c6
Fixed indentation.
2015-10-28 16:26:45 +01:00
Markus Blatt
f447cf648a
fix compilation of flow_solvent.
2015-10-27 17:13:01 +01:00
Markus Blatt
e555cd45f1
Correctly compute the scaling factor for the equations in parallel.
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When running parallel one cannot use Eigen::Array::mean() for this
as the it is just a local part of the complete array. With this commit
we correctly compute the number of global cells in the grid and use this
together with a parallel reduction to compute a global mean value.
2015-10-27 01:58:16 +01:00
Atgeirr Flø Rasmussen
df668cc5e7
Merge pull request #497 from andlaus/error_macros_to_opm_common
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Error macros to opm common
2015-10-12 13:31:54 +02:00
Andreas Lauser
72b0cb2c3e
use the error macros from opm-common
2015-10-08 12:08:28 +02:00
Atgeirr Flø Rasmussen
9e3d360b5b
Silence warnings (shadowing and unused argument).
2015-10-07 10:07:45 +02:00
Tor Harald Sandve
dff77afff7
Use getConvergence and convergenceReduction from base
2015-10-06 11:04:34 +02:00
Tor Harald Sandve
60a6451a6f
Fix typo
2015-10-06 10:40:18 +02:00
Tor Harald Sandve
6106d560ba
Compute matbal_scale for the solvent model
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The material balance scaling is extended to the solvent model
The gas value is used as default and an updateEquationsScaling() method
is added.
Minor modifications is done to the BlackoilModelBase.hpp and
BlackoilModelBase_impl.hpp in order to re-use code from the base case.
2015-10-06 10:40:18 +02:00
Tor Harald Sandve
fb9e21d695
Add a local version of computeWellConnectionPressures()
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Solvent is accounted for in the calculations of well connection
pressures by adjusting the surface_density and the b-factor
TODO: Restructuring to avoid code duplication with
BlackoilModelBase_impl
2015-10-06 10:38:36 +02:00
Tor Harald Sandve
c9b6db6c7e
Use a weighted sum of the b-factors of gas and solvent
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A weighted sum of the b-factors of gas and solvent is used in the well
equation.
2015-10-06 10:33:17 +02:00
Tor Harald Sandve
08ce231869
Recalculate gas fluxes
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The gas fluxes must be recalculated along with the mobilities after the
gasRelPermMultiplier is applied
2015-10-06 10:33:17 +02:00
Tor Harald Sandve
853e1f0dc1
Use ADB for solvent fraction
2015-10-06 10:33:17 +02:00
Tor Harald Sandve
3a78cd4635
BUGFIX Fix out of bounds error
2015-09-03 09:33:46 +02:00
babrodtk
5b287e0ea8
Fixed warnings
2015-09-02 13:02:27 +02:00
Tor Harald Sandve
554f1ec9c6
Add comments to the well equations
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Gas and solvent is combinded and solved together
The input in the well equation is then the
total gas phase = hydro carbon gas + solvent gas
This may need to be reconsidered later, as the model
is tested.
2015-08-18 07:24:08 +02:00
Tor Harald Sandve
cca5410ebb
Fix minor comments in PR#425
2015-08-18 07:24:08 +02:00
Tor Harald Sandve
3b99338bd0
Rename Extended to Solvent
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- classes and files are renamed to use solvent instead of extended in
their names.
2015-08-18 07:24:08 +02:00
