1) Use the solution variable directly in RelativeChange(...)
2) Add a method in the RateConverter that takes the simulator instead of the state.
3) Pass the reservoir pressure directly to the well initialization.
4) Move convertInput(...) to SimulatorFullyImplicitBlackoilEbos.hpp.
This code is only used to convert the initial reservoir state.
5) Modify updateState(...). The solution variable is updated directly and adaptPrimaryVariable(...)
from ewoms is used to switch primary variables. An epsilon is passed to adaptPrimaryVarible(...) after a switch
of primary variables to make it harder to immediately switch back.
The following code used by flow_ebos still uses the reservoirState
1) the initialization
2) restart
3) output of the initial state
4) the step methods in AdaptiveTimeStepping and NonlinearSolver.
The reservoirState is not used by this methods, so after the initial step, an empty reservoirState is passed around in the code.
- add dss to appleyard chopping
- support for bhp injectors with solvent
- copy perfSolventRates between the time steps.
- fix bug in well access indicies when numComponents ~= numPhases
1) Extends the well model to account for solvent surface volumes
2) Add solvent to updateState
3) Add solvent to well and field output
The solvent parts is encapsled in if (has_solvent_) and should not effect
the standard runs.
the compiler suggested braces around the conditions, and by look of
it, it was right: these asserts most likely want express that only the
threephase case or the twophase case without gas are handled...
this changes the conversion of the results to hopefully make it work
with twophase simulations. Note that flow_ebos still does not work
because there is a crash in the well model that I don't understand
(and also, I've disabled an assertation in the well model plus I'm not
completely sure if the conversion code need to do something about the
primary variables in the twophase case).
