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179a03144f
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115 Commits

Author SHA1 Message Date
Kai Bao
179a03144f more bug fixing 
mainly to recover the runnign related to group control example
 2018-05-28 16:05:02 +02:00
Kai Bao
1d218d2fe4 small bug fixes. 2018-05-28 16:05:02 +02:00
Kai Bao
3b70f5004f adding assembleControlEq to StandardWell 
solvent model needs to be handled for the injector control.
 2018-05-28 16:05:02 +02:00
Kai Bao
62947c85b9 updating updatePrimaryVariablesNewton with new primary variables. 2018-05-28 16:05:02 +02:00
Kai Bao
6066884a3d refactoring updateWellState in StandardWell to be two functions 
for other use.
 2018-05-28 16:05:02 +02:00
Kai Bao
eb851b6580 adding BHP to the primary variables for StandardWell 2018-05-28 16:05:02 +02:00
Tor Harald Sandve
54c8a48481 code clean-up based on review 2018-05-08 10:22:47 +02:00
Tor Harald Sandve
f00ad22d98 Fix thermal debug run 2018-05-02 09:15:52 +02:00
Tor Harald Sandve
ee88790dea Add a flow specialization for blackoil with energy conservation 
The energy conservation is enabled by specifying either TEMP or
THERMAL in the deck. The deck also needs to contatin relevant fluid and rock
heat properties.

The blackoil + energy equations are solved fully implicit.
 2018-04-30 13:45:18 +02:00
Arne Morten Kvarving
fddad72a3e fixed: quell signed/unsigned comparison warning 2018-04-13 11:25:10 +02:00
Kai Bao
ed49fd1e88 adapting to the change related to VFP from the parser. 2018-04-11 09:22:52 +02:00
Markus Blatt
01b25f27ed Allow to add well contributions to both matrix and preconditioner matrix. 
matrix_add_well_contributions=true will add to both the preconditioner matrix
and the matrix of the linear operator. preconditioner_add_well_contributions=true
will only add the contributions to the preconditioner matrix.
 2018-03-05 16:48:10 +01:00
Markus Blatt
f07874cf42 Cleanup code. 
Removed unused boolean switch in WellModelMatrixAdapter and removed commented code.
 2018-03-02 20:57:10 +01:00
Atgeirr Flø Rasmussen
b276aaa16b Changes made to test variations of matrix vs matrixless(ish) operator. 2018-03-02 14:22:59 +01:00
Kai Bao
ec8dc4f534 trying to fix a problematic situation when updateWellState 
for example, distr = 0 1 0, for rate control, F = 1 0 0, we will get a
zero F_target, then it is wrong to do the division with F_target.

It is okay when target = 0. When target != 0, the result is already very
wrong. Non-linear iteration can send us anywhere, not sure the best
solution for this kind of strange situation.
 2018-02-28 09:47:22 +01:00
Markus Blatt
44d31f9dcc Removed unused variable warning in addWellContributions. 2018-02-26 16:23:13 +01:00
Markus Blatt
3be954fe98 Move multMatrixTransposed for better testability. 
Otherwise we need to deal with the property system of ewoms.
 2018-02-26 15:49:59 +01:00
Markus Blatt
455cf79d8d Fixed comments in StandardWell 2018-02-26 15:16:07 +01:00
Markus Blatt
8e78f02230 Use Dune::FMatrixHelp::invertMatrix for inversion 
Thus we always take advantage of the specializations in ISTLSolver.hpp
and do need to take care about the type of the matrix block.
 2018-02-26 15:12:14 +01:00
Markus Blatt
b5d55b9fb2 Fix indentation and whitespace. 2018-02-26 14:35:04 +01:00
Markus Blatt
01b90bce05 Improve well matrix products 2018-02-26 14:35:04 +01:00
Markus Blatt
799cbb4b62 Add influences by well perforations to matrix. 
This is only done upon request and uses the auxiliary module approach
provided by ewoms.

In the case of adding the influences we do not execute applyWellModelScaleAdd
or applyWellModel in the operator
 2018-02-26 14:35:04 +01:00
Kai Bao
a8f560b046 addressing the comments. 2018-02-21 14:45:22 +01:00
Kai Bao
89bb589755 update the reservoir volume in WellState 2018-02-21 12:20:43 +01:00
Kai Bao
abfe9d445b recoring solution gas rate and solutiion oil rate in StandardWell 2018-02-21 12:20:43 +01:00
Andreas Lauser
7f3a9f1f43 catch NumericalIssue instead of NumericalProblem 
the underlying problem is that the OPM build system does not define a
HAVE_OPM_COMMON macro in config.h.
 2018-02-08 12:02:25 +01:00
Tor Harald Sandve
969d8f238d Use phase and comp info from FluidSystem 
TODO: The output, fip and restart still uses a mixture of old and
new phase indices. This needs to be adressed in future PRs
 2018-01-03 08:44:37 +01:00
Kai Bao
9317c1f023 removing the current argument in updateWellStateWithTarget 
and some other cleaning up.
 2017-11-30 17:14:29 +01:00
Kai Bao
ea3cbd1fe8 removing numComponents() from WellInterface 
which is dumplicated from BlackoilWellModel.
 2017-11-30 16:31:48 +01:00
Kai Bao
7b61f3e692 moving polymer related to updateWaterMobilityWithPolymer 
in StandardWell.

And not calculating the shear effect for the injecting wells when the
injection wells do not inject polymer.
 2017-11-27 09:24:02 +01:00
Tor Harald Sandve
dd97fc8908 Some clean up. 2017-11-23 11:15:50 +01:00
Tor Harald Sandve
c076ed6485 Move Rateconverter and pvtIdx to the wellInterface 2017-11-23 08:37:30 +01:00
Tor Harald Sandve
054361d537 Make it possible to combine solvent and RESV 
Compute the conversion factor for solvent using the RateConverter.hpp
 2017-11-22 15:21:21 +01:00
Kai Bao
8274fc9275 replacing BlackoilPhases:: with Oil Water Gas in well model 
and also WellStateFullyImplicitBlackoil.

There are more places to do so, while it might be easier to create a
header file for this.
 2017-11-16 12:08:58 +01:00
Kai Bao
ba8eb708d1 fixing reviewing comments from PR 1279. 2017-10-16 17:01:15 +02:00
Kai Bao
1a7b5571b6 trying to add an inner well iteration to speed up convergence. 2017-10-12 14:10:24 +02:00
Kai Bao
dd9ad42a28 correcting the size of seg_comp_initial_ based on num_comp 
for standards wells, all the three equations are mass balance
equatiions, it is safe to use numWellEq.

for MS wells, there is one extra pressure equation, it should be the
number of mass balance equations. If we do not put the polymer equation
inside the well equations, we will face dilemma soon.
 2017-10-12 13:37:05 +02:00
Kai Bao
f7e1623b7a only clearing matrix B and C when only_wells false. 
to save a little calculation.
 2017-10-12 13:37:05 +02:00
Kai Bao
7b873d97c9 small improvements in StandardWell 
there is not functional change.
 2017-10-12 13:37:05 +02:00
Kai Bao
3e2a34239c removing two functions from WellInterface 
computeWellConnectionPressures() and computeAccumWell().
They belongs to the implementation details of well models now.
 2017-10-12 13:37:05 +02:00
Kai Bao
8922f3e041 adding a function calculateExplictQuantities to WellInterface 
to hide some implementation details.
 2017-10-12 13:37:05 +02:00
Kai Bao
47c7c54548 making the updateWellControl to WellInterface 
instead of having two of them in StandardWell and MultisegmentWell
 2017-10-12 13:37:05 +02:00
Kai Bao
359de15f2b begining MultisegmentWell.hpp 2017-10-12 13:36:27 +02:00
Arne Morten Kvarving
a0b81a131a quell signed/unsigned mismatch warning 2017-10-09 14:45:08 +02:00
Arne Morten Kvarving
35fbe03ca7 remove unused variables 
quells warnings
 2017-10-05 12:02:10 +02:00
Atgeirr Flø Rasmussen
f7529cf33e Merge pull request #1269 from GitPaean/fixing_well_efficiency 
correcting the way to use efficiency factor in assembleWelEq
 2017-09-25 10:26:55 +02:00
Tor Harald Sandve
5839962e31 Some trivial cleaning 2017-09-21 12:16:46 +02:00
Tor Harald Sandve
992ab84435 Remove support and tests for pseudo 2p model in flow ebos 2017-09-20 08:11:44 +02:00
Tor Harald Sandve
69c608829f Include RESV in the scaling factor 
- solvent + RESV is not correct. Make the simulator throw until this is
sorted out.

- remove unused parameter
 2017-09-18 11:28:13 +02:00
Tor Harald Sandve
352dccd5e9 Make 2p gas oil compile and runs 
-- use mapping from canonicalToActiveCompIdx from Ebos
-- add guards againts non-existing components
 2017-09-18 11:28:13 +02:00