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77 Commits

Author SHA1 Message Date
Tor Harald Sandve
50c1a1404a Remove BlackoilSolventState 
The solvent saturation is added to BlackoilState and the
BlackoilSolventState is thus redundant.
 2017-05-30 14:22:19 +02:00
Tor Harald Sandve
a5fed26486 BUGFIX Don't try to compute effective properties for FIP if no solvent 2017-05-15 10:13:22 +02:00
Atgeirr Flø Rasmussen
fff99360b3 Workaround: ensure properties necessary for FIP are computed. 
Should only result in an extra call the first time in this function.
 2017-04-25 09:31:48 +02:00
Tor Harald Sandve
ac36ad5ad1 BUGFIX. Store soMax also for the solvent model 2017-04-06 14:39:30 +02:00
Andreas Lauser
ef731672c9 remove the BlackoilPropsAdInterface abstraction layer 
instead, directly use BlackoilPropsAdFromDeck.
 2017-01-02 13:19:23 +01:00
Atgeirr Flø Rasmussen
67374531e3 Merge pull request #880 from totto82/appelyard_fixes 
Fixes in the Appelyard in updateState and updateWellState
 2016-12-15 21:24:11 +01:00
Tor Harald Sandve
4f052e466b Fixes in solvent model related to handling vapoil in the well model 
Tested on SPE5 and Model2
 2016-12-12 10:12:39 +01:00
Tor Harald Sandve
e614c42818 Avoid hard-coded appelyard parameter in flow_ebos 
Start using the parameters in the parameter file instead of the hard-
coded ones.
Unify the restriction of the drs and drv in black-oil and black-oil-
solvent updateState
 2016-12-05 13:44:33 +01:00
Tor Harald Sandve
6e03b9706f Apply Appleyard fixes to solven model 
Tested on SPE5 and Model2 + co2
 2016-12-05 13:44:33 +01:00
Jørgen Kvalsvik
1c6a4b34da Update to shared_ptr-less parser interface. 2016-10-20 14:08:04 +02:00
Andreas Lauser
d76bf11902 adapt to the removal of the unit system of opm-core 
the one which is in opm-parser is now a drop-in replacement.
 2016-10-10 17:00:09 +02:00
Tor Harald Sandve
09a86747b5 Feed solvent wellrates to data::wells for summary output 2016-09-30 09:49:16 +02:00
Tor Harald Sandve
cb5238f5dc BUGFIX 
Updated solvent model after #825
Store rsSat and rvSat in simulator container for outut.
 2016-09-19 11:10:14 +02:00
babrodtk
739976535f Added rs and rv output capabilities 2016-09-07 14:55:53 +02:00
Kai Bao
0ebd25f66a fixing the compilation error due to rebasing. 2016-05-23 15:42:05 +02:00
Kai Bao
879f127ae8 moving variableStateExtractWellsVars() from models to Well Models. 2016-05-23 15:11:52 +02:00
Kai Bao
184bff95ba using well_model_ to represent the WellModel member 2016-05-23 15:11:51 +02:00
Kai Bao
06775ee02c Make BlackoilMultisegmentModel constructured from MultisegmentWells 
Instead of being coustructed based StandardWells and having a
MultisegmentWells member.
 2016-05-23 15:11:51 +02:00
Kai Bao
508de4dc37 adding extractWellPerfProperties to MultisegmentWells 
removing extractWellPerfProperties in all the model classes.
 2016-05-23 15:11:51 +02:00
Tor Harald Sandve
cc2a7d8767 Cleanup in updateState in the solvent model 2016-05-19 12:38:44 +02:00
Tor Harald Sandve
0730ffcb69 BUGFIX. Wrong uses of parenthesis in Cramer's rule 2016-05-19 11:28:36 +02:00
Tor Harald Sandve
bd0ad6aa5b Adapt to changes related to hydroCarbonState 2016-05-19 11:25:27 +02:00
Tor Harald Sandve
03d6dde203 Convergence improvment in the TL model 
-- division on zero is avoided
-- if no solvent is present, pure values are used for the density and
visocity
 2016-05-19 10:49:22 +02:00
Tor Harald Sandve
8be3ca7557 Support for liveoil in combination with solvent 
- a solvent specific updateState is used to assure that the correct oil
saturation is used to detect phase transision
- presence of gas is compensated for in the oil phase
 2016-05-19 10:49:22 +02:00
Kai Bao
cc79dff708 adding the has_solvent_ flag to StandardWellsSolvent 
flow_solvent is able to run cases without solvent.
 2016-04-21 11:17:39 +02:00
Kai Bao
b82e917b0d improving the initSolvent in StandardWellsSolvent 2016-04-20 14:26:13 +02:00
Kai Bao
5bce482086 fixing the compilation and running of flow_solvent 2016-04-20 14:26:13 +02:00
Kai Bao
19734f2103 adding extractWellPerfProperties to StandardWellsSolvent 
to fix the flow_solvent running.
 2016-04-14 16:05:19 +02:00
Kai Bao
5d99fac207 adding StandardWellsSolvent for Solvent model. 2016-04-14 16:05:18 +02:00
Kai Bao
9972dae32a updating for the comments. 
implement wells(), localWellsActive() and wellsActive() for the
BlackoilModelBase and its derived classed.
 2016-04-06 12:54:01 +02:00
Kai Bao
4ad5d81296 fixing wrong codes from the rebase process and cleanup. 2016-04-06 12:54:01 +02:00
Kai Bao
3947ff5b1d moving localWellsActive and wellsActive to StandardWells 
maybe later it can be something general for different types of wells.
 2016-04-06 12:54:01 +02:00
Kai Bao
48483b23c7 update BlackoilSolventModel to fix the compilation. 2016-04-06 12:54:01 +02:00
Tor Harald Sandve
89e540cb2c Pass solutionState as first parameter 
output parameters go last...
 2016-04-05 08:57:07 +02:00
Tor Harald Sandve
925d0becf3 Fix to make flow_solvent run decks without solvent 2016-04-05 08:57:07 +02:00
Tor Harald Sandve
541475b2db Implement computePropertiesForWellConnectionPressures for solvent model 
The solvent specify part of computeWellConnectionPressures is factored
out to computePropertiesForWellConnectionPressures in order to reuse
the computeWellConnectionPressures from the base model.
 2016-04-05 08:57:07 +02:00
Tor Harald Sandve
7b81facfb0 Make use of extractWellPerfProperties to avoid code duplication 
The following changes are done in order to remove the duplicated code in
assemble().
- extractWellPerfProperties takes SolutionState as input (only used in
the solvent model)
- the computation of effective parameters is moved to computeAccum()
With these changes the solvent model can use assemble() from the base
model.
 2016-04-05 08:53:09 +02:00
Tor Harald Sandve
a02a07289e Implement pressure effects in the Todd-Longstaff mixing parameter 
The Todd-Longstaff model is extended to incorporate pressure effects
The solvent viscosity is then caculated as

mu_eff = mu_s^(1-\alpha * \omega) * mu_mix^(\alpha * \omega)

where \omega accounts for the porous media effects and \alpha =
\alpha(pressure) accounts for the miscibility of the solvent and oil
when contacted.
The \alpha values can be given using the TLPMIXPA keyword

If no entries are given to TLPMIXPA the table specified using PMISC will
be used as default.
IF TLPMIXPA does not appear in the grid \alpha = 1 and the pressure
effect is neglected.
This is tested in test_solventprops_ad.cpp
 2016-04-01 15:55:56 +02:00
Atgeirr Flø Rasmussen
8c9b17b943 Merge pull request #615 from totto82/fixes_solvent_model 
Fixes to the solvent model
 2016-04-01 13:40:00 +02:00
Joakim Hove
18c07d5d66 Replaced SimulatorState -> SimulationDataContainer 2016-03-29 10:48:36 +02:00
Tor Harald Sandve
753909b8b9 Fix convergence issues for negative relperm endpoints. 
The relative permeabilty endpoints are scaled by the miscibility
function. The endpoints is not supposed to be negative therefore all
negative values are replaced by zero.
 2016-03-16 11:04:56 +01:00
Tor Harald Sandve
948d985f56 Add support for PMISC 
Pressure effects are added to relative permeability, capillary pressure,
viscosity and density miscibility
 2016-03-04 11:34:31 +01:00
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 
- 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 
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