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Author SHA1 Message Date
Paul Egberts
d2d86e250b added throw when wrong saturation family is specified 2021-03-22 09:59:21 +01:00
Paul Egberts
fc2524a57a fix to allow running a one-phase system 2021-03-19 10:18:04 +01:00
Paul Egberts
eea578a0ef small clean up 2021-03-16 10:21:37 +01:00
Paul Egberts
249983c52a fix to avoid reading gaswater parameters if oil is present 2021-03-11 16:07:53 +01:00
Paul Egberts
809c1d3f1b fix of the wrong number of template arguments error in test_fluidmatrixintercations.cpp 2021-03-11 16:07:53 +01:00
Paul Egberts
ace2930603 use of normalizeKrValues() to account for TOLCRIT 2021-03-11 16:07:52 +01:00
Paul Egberts
b2ce73012e Adaptations neededed for gas-water system 2021-03-11 16:07:52 +01:00
Bård Skaflestad
1479adf6af Explicitly Prevent Negative 3-p Kro Values in Stone 2 Model 
This makes the material balance equations converge more smoothly in
corner cases and makes a real field case run at all.
 2021-02-23 09:17:13 +01:00
Tor Harald Sandve
372bb122a6 Merge pull request #448 from totto82/addExtrapolationThermalVisc 
Extrapolate oil viscosity temperature factor for undersaturated case
 2021-02-23 08:52:01 +01:00
Tor Harald Sandve
ea03ba8287 Extrapolate oil viscosity temperatuer factor for undersaturated case 2021-02-22 15:31:13 +01:00
Bård Skaflestad
c7317befa7 Merge pull request #443 from totto82/blackoilDiff 
Add support for diffusion in the blackoil fluid system
 2021-02-18 18:05:15 +01:00
Tor Harald Sandve
ac4a3871ef Add expression that return diffusion coefficient based on temperature, pressure and salinity 
Diffusion coefficient of CO2 in pure water according to (McLachlan and Danckwerts, 1972)
Diffusion coefficient of CO2 in the brine phase modified following (Ratcliff and Holdcroft,1963 and Al-Rawajfeh, 2004)
 2021-02-12 12:18:07 +01:00
Tor Harald Sandve
f9552a2081 fix assert statement 2021-02-04 09:44:56 +01:00
Tor Harald Sandve
e55568a646 dont allow for default molar weight in DIFFC table 2021-02-04 09:44:56 +01:00
Tor Harald Sandve
f406ecd914 fix molar weights 2021-02-04 09:44:56 +01:00
Tor Harald Sandve
570ec20598 init diffusion from deck 2021-02-04 09:44:56 +01:00
Tor Harald Sandve
ceb71c53a2 Add diffusion to blackoil fluidsystem. Diffusion coefficients are only implemented for the CO2-Brine system 2021-02-04 09:44:56 +01:00
Bård Skaflestad
d10786a18c Merge pull request #439 from bska/vscale-disp-sat-general 
Implement Three-Point Vertical Scaling for Non-Wetting Phase Relative Permeability
 2021-01-27 21:27:47 +01:00
Bård Skaflestad
a56df026be Implement Three-Point Vertical Scaling for Krn 
This commit implements the vertical scaling mode activated by the
keywords KRORW, KRORG, and KRGR.  This is the same scaling mode as
the KRWR feature implemented, but requires reversing the logic since
we implement the non-wetting phase's relative permeability function
in terms of the wetting phase's saturation.
 2021-01-27 18:34:24 +01:00
Bård Skaflestad
2f07358322 Honour TOLCRIT for Tabulated Relative Permeability 
This commit ensures that we honour TOLCRIT settings when
constructing the internal representations of tabulated relative
permeability functions.  In particular, relative permeability values
less than or equal to TOLCRIT are treated as zero.
 2021-01-27 18:34:24 +01:00
Bård Skaflestad
a5a45e4020 Merge pull request #438 from bska/fix-famI-sogcr 
Fix Family I SOGCR Endpoint Hack
 2021-01-27 18:29:57 +01:00
Bård Skaflestad
c390e356f3 Fix Family I SOGCR Endpoint Hack 
The maximum attainable oil saturation in the G/O system is 1-SWL.
Update call sites accordingly.
 2021-01-25 20:37:54 +01:00
Bård Skaflestad
247ce0e3fa Mark Objects 'const' Where Possible 
Also, don't use lifetime extension for 'Evaluation' objects where
these are constructed inside functions.  Doing so inhibits NRVO.
 2021-01-25 20:37:54 +01:00
Tor Harald Sandve
f8f1bfc341 Merge pull request #444 from totto82/addInternalEnergy3 
add missing internal energy function in CO2-Brine module
 2021-01-25 14:12:00 +01:00
Tor Harald Sandve
61d262684d add missing internal energy function in CO2-Brine module 2021-01-21 15:11:10 +01:00
Bård Skaflestad
d0bc4a2c05 Merge pull request #442 from totto82/co2outofidx 
fix out of bound in CO2.hpp

Closes #441.
 2021-01-19 12:39:04 +01:00
Tor Harald Sandve
f528b2c33f fix out of bound in CO2.hpp 2021-01-18 10:12:30 +01:00
Bård Skaflestad
292ee5174a Merge pull request #436 from bska/vscale-disp-sat 
Implement KRWR Vertical Scaling
 2021-01-14 14:15:46 +01:00
Bård Skaflestad
5a30a49e53 Implement KRWR Vertical Scaling 
This commit adds support for scaling of the relative permeability
value for water at the residual saturation of the displacing
(non-wetting) phase.  We use pure vertical scaling in the left
interval [SWL, SR], and a linear/affine function in the right
interval [SR, SWU].
 2021-01-13 15:38:34 +01:00
Bård Skaflestad
d1ccb8fcee Capture Three-Point Vertical Scaling Properties 
These scale relative permeability function values at the residual
saturation of the displacing phase.
 2021-01-13 15:38:34 +01:00
Bård Skaflestad
bb191a5381 Always Store Three Saturation End-Points 
The two-point scalings will use [0] and [2] instead of [0] and [1].
This is in preparation of introducing 'KRWR' scaling which does not
necessarily require the alternative scaling method ('SCALECRS') for
the horizontal direction.
 2021-01-13 15:38:34 +01:00
Atgeirr Flø Rasmussen
bc70036de5 Merge pull request #440 from totto82/fixIdxSalinity 
fix the index into salinity in the BrineCo2Pvt model
 2021-01-13 15:01:54 +01:00
Tor Harald Sandve
474d8c72c5 fix the index into salinity in the BrineCo2Pvt model 2021-01-13 12:35:04 +01:00
Joakim Hove
f4cb4dc292 Merge pull request #437 from joakim-hove/sched-oilvap 
Get OilVaporization properties from ScheduleState
 2021-01-08 09:21:36 +01:00
Joakim Hove
a431e8ba7f Get OilVaporization properties from ScheduleState 2021-01-07 09:20:19 +01:00
Bård Skaflestad
3db77dd5f9 Merge pull request #434 from bska/use-common-eps-api 
Extract Endpoints Using Common Facilities
 2021-01-05 11:52:52 +01:00
Bård Skaflestad
51e2efd431 Get Saturation Function Family From SatFuncControls 
There's no need to duplicate this logic.
 2020-12-21 00:51:36 +01:00
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