本文整理汇总了C++中BaseType::bhp方法的典型用法代码示例。如果您正苦于以下问题：C++ BaseType::bhp方法的具体用法？C++ BaseType::bhp怎么用？C++ BaseType::bhp使用的例子？那么, 这里精选的方法代码示例或许可以为您提供帮助。您也可以进一步了解该方法所在类BaseType的用法示例。
在下文中一共展示了BaseType::bhp方法的1个代码示例，这些例子默认根据受欢迎程度排序。您可以为喜欢或者感觉有用的代码点赞，您的评价将有助于系统推荐出更棒的C++代码示例。
示例1: setWellSolutions
/// Set wellSolutions() based on the base class members.
void setWellSolutions(const PhaseUsage& pu)
{
// Set nw and np, or return if no wells.
if (wells_.get() == nullptr) {
return;
}
const int nw = wells_->number_of_wells;
if (nw == 0) {
return;
}
const int np = wells_->number_of_phases;
well_solutions_.clear();
well_solutions_.resize(nw * np, 0.0);
std::vector<double> g = {1.0,1.0,0.01};
for (int w = 0; w < nw; ++w) {
WellControls* wc = wells_->ctrls[w];
// The current control in the well state overrides
// the current control set in the Wells struct, which
// is instead treated as a default.
const int current = currentControls()[w];
well_controls_set_current( wc, current);
const WellType& well_type = wells_->type[w];
switch (well_controls_iget_type(wc, current)) {
case THP: // Intentional fall-through
case BHP:
if (well_type == INJECTOR) {
for (int p = 0; p < np; ++p) {
well_solutions_[w] += wellRates()[np*w + p] * wells_->comp_frac[np*w + p];
}
} else {
for (int p = 0; p < np; ++p) {
well_solutions_[w] += g[p] * wellRates()[np*w + p];
}
}
break;
case RESERVOIR_RATE: // Intentional fall-through
case SURFACE_RATE:
wellSolutions()[w] = bhp()[w];
break;
}
double total_rates = 0.0;
for (int p = 0; p < np; ++p) {
total_rates += g[p] * wellRates()[np*w + p];
}
const int waterpos = pu.phase_pos[Water];
const int gaspos = pu.phase_pos[Gas];
assert(np == 3 || (np == 2 && !pu.phase_used[Gas]));
// assumes the gas fractions are stored after water fractions
if(std::abs(total_rates) > 0) {
if( pu.phase_used[Water] ) {
wellSolutions()[nw + w] = g[Water] * wellRates()[np*w + waterpos] / total_rates;
}
if( pu.phase_used[Gas] ) {
wellSolutions()[2*nw + w] = g[Gas] * wellRates()[np*w + gaspos] / total_rates ;
}
} else {
if( pu.phase_used[Water] ) {
wellSolutions()[nw + w] = wells_->comp_frac[np*w + waterpos];
}
if( pu.phase_used[Gas] ) {
wellSolutions()[2*nw + w] = wells_->comp_frac[np*w + gaspos];
}
}
}
}