OilfieldToolsNet/opm-common
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Author SHA1 Message Date
Bård Skaflestad
15c84cc3fc Extract Endpoints Using Common Facilities 
This means we get the "SWCO" handling in SOGCR based on SGOF for
free, and also removes duplicated and complex logic.
 2020-12-21 00:51:36 +01:00
Bård Skaflestad
fb5bdc1302 EPS Grid Properties: Prefer Single Assignments 2020-12-11 12:11:14 +01:00
Atgeirr Flø Rasmussen
ce4cbafe95 Merge pull request #435 from akva2/test_init 
Change static intialization of CO2 tables to avoid function call, use construction.
 2020-12-11 07:34:52 +01:00
Arne Morten Kvarving
75b2609336 test if apple clang likes this better 2020-12-08 15:27:50 +01:00
Atgeirr Flø Rasmussen
e58a660235 Merge pull request #432 from goncalvesmachadoc/aquifer 
Do not check for kr curves for water single-phase
 2020-12-01 08:38:02 +01:00
Cintia Goncalves Machado
5513bff1ba generalize single-phase fix 2020-11-25 17:48:45 +01:00
Cintia Goncalves Machado
1d4dd874ca do not check for kr curves for flow_onephase 2020-11-24 17:38:12 +01:00
Arne Morten Kvarving
2e7b1e4339 Merge pull request #430 from akva2/janitoring 
fix header guard
 2020-10-05 12:46:15 +02:00
Arne Morten Kvarving
d3a226166f fix header guard 2020-10-05 11:04:48 +02:00
Tor Harald Sandve
28dd5a2b36 Merge pull request #427 from totto82/co2pvt 
Add a co2brine pvt model
 2020-10-02 12:26:19 +02:00
Tor Harald Sandve
15ff65ffcd Add a co2brine pvt model 
The CO2BRINE model is activated by setting CO2STOR in the RUNSPEC section

The CO2 and brine pvt properties are computed based on pvt models in opm-material
- CO2 density is from Span and Wager (1996) as given in co2table.inc
- CO2 viscosity is from Fenhour et al (1998)
- Brine density and viscosity is based on H20 + correction based on Batzle and Wang (1992)
- H20 density is from Hu et al (2007)
- H20 viscosity is computed from density based on correlation given in IAPWS 97

At the current stage the oil-phase is used to model the brine. If a proper gas-water
simulator is made, the Brine PVT should be moved to the water phase.

Known limitations:
- Currently the viscosity of the Brine does not depend on the composition
- Salinity is assumed to be constant and given by SALINITY [mol/kg].
 2020-10-01 16:15:39 +02:00
Joakim Hove
e54ff1af09 Merge pull request #428 from joakim-hove/remove-common-exceptions 
Remove unusued #include common excpetions
 2020-09-21 14:27:34 +02:00
Joakim Hove
1315acfe51 Remove unusued #include common excpetions 2020-09-21 10:56:05 +02:00
Bård Skaflestad
a068071f88 Merge pull request #425 from goncalvesmachadoc/patch-3 
Extrapolate GASVISCT
 2020-08-22 00:12:38 +02:00
Bård Skaflestad
d846c7128a Merge pull request #424 from goncalvesmachadoc/patch-2 
Extrapolate OILVISCT
 2020-08-22 00:10:44 +02:00
Cintia Goncalves Machado
d4f6ed4366 Extrapolate GASVISCT 
Allow for extrapolation of gas viscosity curves.
 2020-08-06 17:26:14 +02:00
Cintia Goncalves Machado
2ac7f84b9f Extrapolate OILVISCT 
Allow for extrapolation of oil viscosity curves
 2020-08-06 17:20:58 +02:00
Bård Skaflestad
50bd881199 Merge pull request #423 from totto82/applyPVTWsalt 
make the water PVT salt dependent
 2020-07-08 09:28:53 +02:00
Tor Harald Sandve
74a6b98b4f fix return type getSaltConcentration 2020-07-08 08:09:26 +02:00
Tor Harald Sandve
b4c8dd5e86 make the water PVT salt dependent 2020-07-02 13:42:58 +02:00
Atgeirr Flø Rasmussen
a11b3a53b2 Merge pull request #422 from goncalvesmachadoc/patch-1 
Allow for extrapolation of WATVISC curve
 2020-06-26 09:55:30 +02:00
Cintia Goncalves Machado
50f0f36156 Allow for extrapolation of WATVISC curve 2020-06-25 14:25:26 +02:00
Atgeirr Flø Rasmussen
1a9c3c30ca Merge pull request #421 from atgeirr/sequential 
Add total saturation and capillary pressure to blackoil fluid state.
 2020-06-11 11:18:50 +02:00
hnil
efb7dce342 Add total saturation and capillary pressure to blackoil fluid state. 
This is intended for use with sequential formulations.
 2020-06-11 08:51:55 +02:00
Atgeirr Flø Rasmussen
1f9c136f20 Merge pull request #420 from atgeirr/add-phaseIsActive 
Add phaseIsActive(unsigned int) to base fluid system (returning true).
 2020-05-29 16:31:59 +02:00
Atgeirr Flø Rasmussen
b5bd0a519f Add phaseIsActive(unsigned int) to base fluid system (returning true). 
This promotes the feature from being a special function for the black oil
fluid system to being in theory available for all. The need for this
arose in downstream code.
 2020-05-29 14:49:59 +02:00
Joakim Hove
12161d9c79 Merge pull request #417 from bska/fix-missing-include 
Grid Properties: Include FieldPropsManager
 2020-04-07 11:49:41 +02:00
Bård Skaflestad
f343e605ea Grid Properties: Include FieldPropsManager 
We use the manager internally (for instance in the try_get() helper
function) and therefore need a declaration in scope.
 2020-04-06 17:30:19 +02:00
Joakim Hove
30cbe6ed25 Merge pull request #415 from joakim-hove/use-shared-ptr 
Use std::shared_ptr for Python handle
 2020-03-31 16:50:47 +02:00
Joakim Hove
68e779a827 Use std::shared_ptr for Python handle 2020-03-31 10:46:17 +02:00
Joakim Hove
0defd3de8e Merge pull request #414 from joakim-hove/add-python-arg 
Add Python arg to Schedule constructor
 2020-03-27 13:43:55 +01:00
Joakim Hove
b68bdea6e4 Add Python arg to Schedule constructor 2020-03-25 18:32:46 +01:00
Bård Skaflestad
778459ec84 Merge pull request #413 from akva2/followup_stonetype 
use relocated KrModel
 2020-03-10 07:58:17 -05:00
Arne Morten Kvarving
51e5574c07 use relocated KrModel 2020-03-10 10:40:09 +01:00
Atgeirr Flø Rasmussen
a003a21d5c Merge pull request #412 from akva2/no_serialization_matman 
Get rid of deck usage setting up MaterialLawManager
 2020-03-09 16:05:40 +01:00
Arne Morten Kvarving
91d4dcdf90 remove serialization templates from EclMaterialLawManager 2020-03-09 11:42:37 +01:00
Arne Morten Kvarving
a2d52da69f rename EclMaterialLawManager::initFromDeck to initFromState 
no deck usage any more
 2020-03-09 11:42:37 +01:00
Arne Morten Kvarving
c85243314b get rid of deck usage setting up EclEpsScalingPointsInfo 2020-03-09 10:28:02 +01:00
Arne Morten Kvarving
477f2cd425 get rid of deck usage setting up EclEpsConfig 2020-03-09 10:28:02 +01:00
Arne Morten Kvarving
8d07bef17c get rid of deck usage setting up three phase options 2020-03-09 10:10:32 +01:00
Arne Morten Kvarving
e0a43d7973 use hysteresis config from state 2020-03-09 09:33:08 +01:00
Arne Morten Kvarving
5f2d7c6308 use STONE1EX from table manager 2020-03-06 12:17:21 +01:00
Bård Skaflestad
861a6ad4b4 Merge pull request #411 from akva2/no_serialization_fluidsystem 
Get rid of deck usage in BlackoilFluidSystem
 2020-03-03 21:27:04 -06:00
Arne Morten Kvarving
36d9df1876 drop serialization templates for BlackoilFluidSystem 2020-03-03 15:57:58 +01:00
Arne Morten Kvarving
51d644b96c changed: get rid of last deck usage in BlackoilFluidSystem 
rename initFromDeck to initFromState. Pass the Schedule instead
of the deck.
 2020-03-03 15:57:58 +01:00
Arne Morten Kvarving
43232d878f Merge pull request #409 from akva2/less_deck_blackoil_fluid_system 
changed: lessen deck usage setting up BlackoilFluidSystem
 2020-03-03 15:57:05 +01:00
Arne Morten Kvarving
2c270cb4f3 changed: lessen deck usage setting up BlackoilFluidSystem 2020-03-03 15:56:33 +01:00
Arne Morten Kvarving
24e84ad2e5 Merge pull request #410 from akva2/use_state_surface_conditions 
use surface conditions from InitConfig
 2020-03-03 13:46:14 +01:00
Arne Morten Kvarving
3dc71ffb5b use standard conditions from EclipseState 2020-03-03 12:03:48 +01:00
Markus Blatt
fb803f1fec Merge pull request #408 from akva2/use_compressed_props 
Use compressed field properties
 2020-03-02 09:46:16 +01:00