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small bug fixes.

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This commit is contained in:
Kai Bao
2018-05-09 15:07:43 +02:00
parent 3b70f5004f
commit 1d218d2fe4
2 changed files with 19 additions and 21 deletions
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25
opm/autodiff/StandardWell.hpp
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@@ -57,6 +57,12 @@ namespace Opm
using Base::has_polymer;
using Base::has_energy;
// polymer concentration and temperature are already known by the well, so
// polymer and energy conservation do not need to be considered explicitly
static const int numPolymerEq = has_polymer ? 1 : 0;
static const int numEnergyEq = has_energy ? 1 : 0;
static const int numWellEq = numEq + 1 - numPolymerEq - numEnergyEq;
// the positions of the primary variables for StandardWell
// there are four primary variables, the second and the third ones are F_w and F_g
// the first one is the weighted total rate (G_t), the second and the third ones are F_w and F_g
@@ -64,17 +70,19 @@ namespace Opm
// the fraction of the solvent, as an extension of the blackoil model, is behind the BHP
// correspondingly, we have four well equations for blackoil model, the first three are mass
// converstation equations, and the last one is the well control equation.
// primary variables related to other components, will be before the Bhp and after F_g.
// well control equation is always the last well equation, other equations will be before the
// well control equation and are conservation equations for components involved.
// TODO: in the current implementation, we use the well rate as the first primary variables for injectors
// TODO: not sure we should change it.
static const bool gasoil = numEq == 2 && (Indices::compositionSwitchIdx >= 0);
static const int GTotal = 0;
static const int WFrac = gasoil? -1000: 1;
static const int GFrac = gasoil? 1: 2;
// TODO: it is possible the order of Bhp and SFrac need to switched, due to scalingFactor function
// TODO: we will do that when we see the problem.
static const int Bhp = gasoil? 2 : 3;
static const int SFrac = !has_solvent ? -1000 : Bhp + 1;
static const int SFrac = !has_solvent ? -1000 : 3;
// the index for Bhp in primary variables and also the index of well control equation
// they both will be the last one in their system.
static const int Bhp = numWellEq - 1;
using typename Base::Scalar;
using typename Base::ConvergenceReport;
@@ -85,11 +93,6 @@ namespace Opm
using Base::Oil;
using Base::Gas;
// polymer concentration and temperature are already known by the well, so
// polymer and energy conservation do not need to be considered explicitly
static const int numPolymerEq = has_polymer ? 1 : 0;
static const int numEnergyEq = has_energy ? 1 : 0;
static const int numWellEq =numEq - numPolymerEq - numEnergyEq;
using typename Base::Mat;
using typename Base::BVector;
using typename Base::Eval;
@@ -239,7 +242,7 @@ namespace Opm
// TODO: this function should be moved to the base class.
// while it faces chanllenges for MSWell later, since the calculation of bhp
// based on THP is never implemented for MSWell yet.
EvalWell getBhp() const;
const EvalWell& getBhp() const;
// TODO: it is also possible to be moved to the base class.
EvalWell getQs(const int comp_idx) const;