3f3b96587b
These properties are actually infinite in the two-phase region, but attempting to compute them by finite difference would incorrectly give a finite result, so they need to be treated as a special case.
806 lines
21 KiB
C++
806 lines
21 KiB
C++
//! @file Sub.cpp
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/*
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* The Substance class
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* D. Goodwin, Caltech Nov. 1996
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*/
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// This file is part of Cantera. See License.txt in the top-level directory or
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// at http://www.cantera.org/license.txt for license and copyright information.
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#include "cantera/tpx/Sub.h"
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#include "cantera/base/stringUtils.h"
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#include "cantera/base/global.h"
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using std::string;
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using namespace Cantera;
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namespace {
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// these correspond to ordering withing propertyFlag::type
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std::string propertySymbols[] = {"H", "S", "U", "V", "P", "T"};
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}
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namespace tpx
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{
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Substance::Substance() :
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T(Undef),
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Rho(Undef),
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Tslast(Undef),
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Rhf(Undef),
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Rhv(Undef),
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Pst(Undef),
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m_energy_offset(0.0),
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m_entropy_offset(0.0),
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kbr(0)
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{
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}
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void Substance::setStdState(double h0, double s0, double t0, double p0)
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{
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Set(PropertyPair::TP, t0, p0);
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double hh = h();
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double ss = s();
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double hoff = h0 - hh;
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double soff = s0 - ss;
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m_entropy_offset += soff;
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m_energy_offset += hoff;
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}
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double Substance::P()
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{
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return TwoPhase() ? Ps() : Pp();
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}
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const double DeltaT = 0.000001;
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double Substance::cv()
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{
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double Tsave = T, dt = 1.e-4*T;
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double x0 = x();
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double T1 = std::max(Tmin(), Tsave - dt);
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double T2 = std::min(Tmax(), Tsave + dt);
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set_T(T1);
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double x1 = x();
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if ((x0 == 1.0 || x0 == 0.0) && x1 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// T-dT is not, just take a one-sided difference
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T1 = Tsave;
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set_T(T1);
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}
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double s1 = s();
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set_T(T2);
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double x2 = x();
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if ((x0 == 1.0 || x0 == 0.0) && x2 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// T+dT is not, just take a one-sided difference
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T2 = Tsave;
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set_T(T2);
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}
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double s2 = s();
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set_T(Tsave);
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return T*(s2 - s1)/(T2-T1);
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}
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double Substance::cp()
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{
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double Tsave = T, dt = 1.e-4*T;
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double T1 = std::max(Tmin(), Tsave - dt);
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double T2 = std::min(Tmax(), Tsave + dt);
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double p0 = P();
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double x0 = x();
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if (TwoPhase()) {
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// In the two-phase region, cp is infinite
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return std::numeric_limits<double>::infinity();
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}
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Set(PropertyPair::TP, T1, p0);
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double x1 = x();
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if (x1 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// T-dT is not, just take a one-sided difference
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T1 = Tsave;
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Set(PropertyPair::TP, T1, p0);
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}
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double s1 = s();
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Set(PropertyPair::TP, T2, p0);
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double x2 = x();
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if (x2 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// T+dT is not, just take a one-sided difference
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T2 = Tsave;
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Set(PropertyPair::TP, T2, p0);
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}
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double s2 = s();
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Set(PropertyPair::TP, Tsave, p0);
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return T*(s2 - s1)/(T2-T1);
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}
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double Substance::thermalExpansionCoeff()
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{
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double Tsave = T, dt = 1.e-4*T;
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double T1 = std::max(Tmin(), Tsave - dt);
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double T2 = std::min(Tmax(), Tsave + dt);
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double p0 = P();
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double x0 = x();
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if (TwoPhase()) {
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// In the two-phase region, the thermal expansion coefficient is
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// infinite
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return std::numeric_limits<double>::infinity();
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}
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Set(PropertyPair::TP, T1, p0);
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double x1 = x();
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if (x1 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// T-dT is not, just take a one-sided difference
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T1 = Tsave;
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Set(PropertyPair::TP, T1, p0);
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}
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double v1 = v();
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Set(PropertyPair::TP, T2, p0);
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double x2 = x();
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if (x2 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// T+dT is not, just take a one-sided difference
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T2 = Tsave;
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Set(PropertyPair::TP, T2, p0);
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}
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double v2 = v();
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Set(PropertyPair::TP, Tsave, p0);
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return 2.0*(v2 - v1)/((v2 + v1)*(T2-T1));
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}
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double Substance::isothermalCompressibility()
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{
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double Psave = P(), dp = 1.e-4*Psave;
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double x0 = x();
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if (TwoPhase()) {
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// In the two-phase region, the isothermal compressibility is infinite
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return std::numeric_limits<double>::infinity();
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}
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double v0 = v();
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double P1 = Psave - dp;
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double P2 = Psave + dp;
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Set(PropertyPair::TP, T, P1);
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double x1 = x();
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if (x1 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// P-dP is not, just take a one-sided difference
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P1 = Psave;
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Set(PropertyPair::TP, T, P1);
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}
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double v1 = v();
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Set(PropertyPair::TP, T, P2);
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double x2 = x();
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if (x2 != x0) {
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// If the initial state was pure liquid or pure vapor, and the state at
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// P+dP is not, just take a one-sided difference
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P2 = Psave;
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Set(PropertyPair::TP, T, P2);
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}
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double v2 = v();
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Set(PropertyPair::TP, T, Psave);
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return -(v2 - v1)/(v0*(P2-P1));
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}
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double Substance::dPsdT()
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{
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double tsave = T;
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double ps1 = Ps();
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T += DeltaT;
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double dpdt = (Ps() - ps1)/DeltaT;
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T = tsave;
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return dpdt;
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}
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int Substance::TwoPhase()
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{
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if (T >= Tcrit()) {
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return 0;
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}
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update_sat();
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return ((Rho < Rhf) && (Rho > Rhv) ? 1 : 0);
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}
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double Substance::x()
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{
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if (T >= Tcrit()) {
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return (1.0/Rho < Vcrit() ? 0.0 : 1.0);
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} else {
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update_sat();
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if (Rho <= Rhv) {
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return 1.0;
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} else if (Rho >= Rhf) {
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return 0.0;
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} else {
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double vv = 1.0/Rhv;
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double vl = 1.0/Rhf;
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return (1.0/Rho - vl)/(vv - vl);
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}
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}
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}
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double Substance::Tsat(double p)
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{
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if (p <= 0.0 || p > Pcrit()) {
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throw CanteraError("Substance::Tsat", "illegal pressure value");
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}
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int LoopCount = 0;
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double tol = 1.e-6*p;
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double Tsave = T;
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if (T < Tmin()) {
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T = 0.5*(Tcrit() - Tmin());
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}
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if (T >= Tcrit()) {
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T = 0.5*(Tcrit() - Tmin());
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}
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double dp = 10*tol;
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while (fabs(dp) > tol) {
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if (T > Tcrit()) {
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T = Tcrit() - 0.001;
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}
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if (T < Tmin()) {
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T = Tmin() + 0.001;
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}
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dp = p - Ps();
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double dt = dp/dPsdT();
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double dta = fabs(dt);
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double dtm = 0.1*T;
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if (dta > dtm) {
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dt = dt*dtm/dta;
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}
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T += dt;
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LoopCount++;
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if (LoopCount > 100) {
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T = Tsave;
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throw CanteraError("Substance::Tsat", "No convergence");
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}
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}
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double tsat = T;
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T = Tsave;
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return tsat;
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}
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// property tolerances
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static const double TolAbsH = 1.e-4; // J/kg
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static const double TolAbsU = 1.e-4;
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static const double TolAbsS = 1.e-7;
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static const double TolAbsP = 0.0; // Pa, this is supposed to be zero
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static const double TolAbsV = 1.e-8;
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static const double TolAbsT = 1.e-3;
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static const double TolRel = 1.e-8;
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void Substance::Set(PropertyPair::type XY, double x0, double y0)
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{
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double temp;
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/* if inverted (PT) switch order and change sign of XY (TP = -PT) */
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if (XY < 0) {
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std::swap(x0, y0);
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XY = static_cast<PropertyPair::type>(-XY);
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}
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switch (XY) {
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case PropertyPair::TV:
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set_T(x0);
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set_v(y0);
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break;
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case PropertyPair::HP:
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if (Lever(Pgiven, y0, x0, propertyFlag::H)) {
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return;
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}
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set_xy(propertyFlag::H, propertyFlag::P,
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x0, y0, TolAbsH, TolAbsP, TolRel, TolRel);
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break;
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case PropertyPair::SP:
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if (Lever(Pgiven, y0, x0, propertyFlag::S)) {
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return;
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}
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set_xy(propertyFlag::S, propertyFlag::P,
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x0, y0, TolAbsS, TolAbsP, TolRel, TolRel);
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break;
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case PropertyPair::PV:
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if (Lever(Pgiven, x0, y0, propertyFlag::V)) {
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return;
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}
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set_xy(propertyFlag::P, propertyFlag::V,
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x0, y0, TolAbsP, TolAbsV, TolRel, TolRel);
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break;
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case PropertyPair::TP:
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if (x0 < Tcrit()) {
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set_T(x0);
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if (y0 < Ps()) {
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Set(PropertyPair::TX, x0, 1.0);
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} else {
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Set(PropertyPair::TX, x0, 0.0);
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}
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} else {
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set_T(x0);
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}
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set_xy(propertyFlag::T, propertyFlag::P,
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x0, y0, TolAbsT, TolAbsP, TolRel, TolRel);
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break;
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case PropertyPair::UV:
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set_xy(propertyFlag::U, propertyFlag::V,
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x0, y0, TolAbsU, TolAbsV, TolRel, TolRel);
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break;
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case PropertyPair::ST:
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if (Lever(Tgiven, y0, x0, propertyFlag::S)) {
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return;
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}
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set_xy(propertyFlag::S, propertyFlag::T,
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x0, y0, TolAbsS, TolAbsT, TolRel, TolRel);
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break;
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case PropertyPair::SV:
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set_xy(propertyFlag::S, propertyFlag::V,
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x0, y0, TolAbsS, TolAbsV, TolRel, TolRel);
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break;
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case PropertyPair::UP:
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if (Lever(Pgiven, y0, x0, propertyFlag::U)) {
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return;
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}
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set_xy(propertyFlag::U, propertyFlag::P,
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x0, y0, TolAbsU, TolAbsP, TolRel, TolRel);
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break;
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case PropertyPair::VH:
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set_xy(propertyFlag::V, propertyFlag::H,
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x0, y0, TolAbsV, TolAbsH, TolRel, TolRel);
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break;
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case PropertyPair::TH:
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set_xy(propertyFlag::T, propertyFlag::H,
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x0, y0, TolAbsT, TolAbsH, TolRel, TolRel);
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break;
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case PropertyPair::SH:
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set_xy(propertyFlag::S, propertyFlag::H,
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x0, y0, TolAbsS, TolAbsH, TolRel, TolRel);
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break;
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case PropertyPair::PX:
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temp = Tsat(x0);
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if (y0 > 1.0 || y0 < 0.0) {
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throw CanteraError("Substance::Set",
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"Invalid vapor fraction, {}", y0);
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} else if (temp >= Tcrit()) {
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throw CanteraError("Substance::Set",
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"Can't set vapor fraction above the critical point");
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} else {
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set_T(temp);
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update_sat();
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Rho = 1.0/((1.0 - y0)/Rhf + y0/Rhv);
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}
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break;
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case PropertyPair::TX:
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if (y0 > 1.0 || y0 < 0.0) {
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throw CanteraError("Substance::Set",
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"Invalid vapor fraction, {}", y0);
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} else if (x0 >= Tcrit()) {
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throw CanteraError("Substance::Set",
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"Can't set vapor fraction above the critical point");
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} else {
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set_T(x0);
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update_sat();
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Rho = 1.0/((1.0 - y0)/Rhf + y0/Rhv);
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}
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break;
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default:
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throw CanteraError("Substance::Set", "Invalid input.");
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}
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}
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//------------------ Protected and Private Functions -------------------
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void Substance::set_Rho(double r0)
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{
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if (r0 > 0.0) {
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Rho = r0;
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} else {
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throw CanteraError("Substance::set_Rho", "Invalid density: {}", r0);
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}
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}
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void Substance::set_T(double t0)
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{
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if ((t0 >= Tmin()) && (t0 <= Tmax())) {
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T = t0;
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} else {
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throw CanteraError("Substance::set_T", "illegal temperature: {}", t0);
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}
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}
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void Substance::set_v(double v0)
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{
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if (v0 > 0) {
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Rho = 1.0/v0;
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} else {
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throw CanteraError("Substance::set_v",
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"negative specific volume: {}", v0);
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}
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}
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double Substance::Ps()
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{
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if (T < Tmin() || T > Tcrit()) {
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throw CanteraError("Substance::Ps",
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"illegal temperature value {}", T);
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}
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update_sat();
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return Pst;
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}
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void Substance::update_sat()
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{
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if ((T != Tslast) && (T < Tcrit())) {
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double Rho_save = Rho;
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double pp = Psat();
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double lps = log(pp);
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// trial value = Psat from correlation
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int i;
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for (i = 0; i<20; i++) {
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if (i==0) {
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Rho = ldens(); // trial value = liquid density
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} else {
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Rho = Rhf;
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}
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set_TPp(T,pp);
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Rhf = Rho; // sat liquid density
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double gf = hp() - T*sp();
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if (i==0) {
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Rho = pp*MolWt()/(GasConstant*T); // trial value = ideal gas
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} else {
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Rho = Rhv;
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}
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set_TPp(T,pp);
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Rhv = Rho; // sat vapor density
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double gv = hp() - T*sp();
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double dg = gv - gf;
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if (Rhv > Rhf) {
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std::swap(Rhv, Rhf);
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dg = - dg;
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}
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if (fabs(dg) < 0.001 && Rhf > Rhv) {
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break;
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}
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double dp = dg/(1.0/Rhv - 1.0/Rhf);
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double psold = pp;
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if (fabs(dp) > pp) {
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lps -= dg/(pp*(1.0/Rhv - 1.0/Rhf));
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pp = exp(lps);
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} else {
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pp -= dp;
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lps = log(pp);
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}
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if (pp > Pcrit()) {
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pp = psold + 0.5*(Pcrit() - psold);
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lps = log(pp);
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} else if (pp < 0.0) {
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pp = psold/2.0;
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lps = log(pp);
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}
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}
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if (Rhf <= Rhv) {
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throw CanteraError("Substance::update_sat",
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"wrong root found for sat. liquid or vapor at P = {}", pp);
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}
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if (i >= 20) {
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throw CanteraError("substance::update_sat","no convergence");
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} else {
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Pst = pp;
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Tslast = T;
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}
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Rho = Rho_save;
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}
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}
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double Substance::vprop(propertyFlag::type ijob)
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{
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switch (ijob) {
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case propertyFlag::H:
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return hp();
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case propertyFlag::S:
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return sp();
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case propertyFlag::U:
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return up();
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case propertyFlag::V:
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return vp();
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case propertyFlag::P:
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return Pp();
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default:
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throw CanteraError("Substance::vprop", "invalid job index");
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}
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}
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int Substance::Lever(int itp, double sat, double val, propertyFlag::type ifunc)
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{
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double psat;
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double Tsave = T;
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double Rhosave = Rho;
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if (itp == Tgiven) {
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if (sat >= Tcrit()) {
|
|
return 0;
|
|
}
|
|
T = sat;
|
|
psat = Ps();
|
|
} else if (itp == Pgiven) {
|
|
if (sat >= Pcrit()) {
|
|
return 0;
|
|
}
|
|
psat = sat;
|
|
try {
|
|
T = Tsat(psat);
|
|
} catch (CanteraError&) {
|
|
// Failure to converge here is not an error
|
|
T = Tsave;
|
|
Rho = Rhosave;
|
|
return 0;
|
|
}
|
|
} else {
|
|
throw CanteraError("Substance::Lever","general error");
|
|
}
|
|
Set(PropertyPair::TX, T, 1.0);
|
|
double Valg = vprop(ifunc);
|
|
Set(PropertyPair::TX, T, 0.0);
|
|
double Valf = vprop(ifunc);
|
|
if (val >= Valf && val <= Valg) {
|
|
double xx = (val - Valf)/(Valg - Valf);
|
|
double vv = (1.0 - xx)/Rhf + xx/Rhv;
|
|
set_v(vv);
|
|
return 1;
|
|
} else {
|
|
T = Tsave;
|
|
Rho = Rhosave;
|
|
return 0;
|
|
}
|
|
}
|
|
|
|
void Substance::set_xy(propertyFlag::type ifx, propertyFlag::type ify,
|
|
double X, double Y,
|
|
double atx, double aty,
|
|
double rtx, double rty)
|
|
{
|
|
double v_here, t_here;
|
|
double dvs1 = 2.0*Vcrit();
|
|
double dvs2 = 0.7*Vcrit();
|
|
int LoopCount = 0;
|
|
|
|
double v_save = 1.0/Rho;
|
|
double t_save = T;
|
|
|
|
if ((T == Undef) && (Rho == Undef)) {
|
|
// new object, try to pick a "reasonable" starting point
|
|
Set(PropertyPair::TV,Tcrit()*1.1,Vcrit()*1.1);
|
|
t_here = T;
|
|
v_here = 1.0/Rho;
|
|
} else if (Rho == Undef) {
|
|
// new object, try to pick a "reasonable" starting point
|
|
Set(PropertyPair::TV,T,Vcrit()*1.1);
|
|
t_here = T;
|
|
v_here = 1.0/Rho;
|
|
} else {
|
|
v_here = v_save;
|
|
t_here = t_save;
|
|
}
|
|
|
|
double Xa = fabs(X);
|
|
double Ya = fabs(Y);
|
|
while (true) {
|
|
double x_here = prop(ifx);
|
|
double y_here = prop(ify);
|
|
double err_x = fabs(X - x_here);
|
|
double err_y = fabs(Y - y_here);
|
|
|
|
if ((err_x < atx + rtx*Xa) && (err_y < aty + rty*Ya)) {
|
|
break;
|
|
}
|
|
|
|
/* perturb t */
|
|
double dt = 0.001*t_here;
|
|
if (t_here + dt > Tmax()) {
|
|
dt *= -1.0;
|
|
}
|
|
|
|
/* perturb v */
|
|
double dv = 0.001*v_here;
|
|
if (v_here <= Vcrit()) {
|
|
dv *= -1.0;
|
|
}
|
|
|
|
/* derivatives with respect to T */
|
|
Set(PropertyPair::TV, t_here + dt, v_here);
|
|
double dxdt = (prop(ifx) - x_here)/dt;
|
|
double dydt = (prop(ify) - y_here)/dt;
|
|
|
|
/* derivatives with respect to v */
|
|
Set(PropertyPair::TV, t_here, v_here + dv);
|
|
double dxdv = (prop(ifx) - x_here)/dv;
|
|
double dydv = (prop(ify) - y_here)/dv;
|
|
|
|
double det = dxdt*dydv - dydt*dxdv;
|
|
dt = ((X - x_here)*dydv - (Y - y_here)*dxdv)/det;
|
|
dv = ((Y - y_here)*dxdt - (X - x_here)*dydt)/det;
|
|
|
|
double dvm = 0.2*v_here;
|
|
if (v_here < dvs1) {
|
|
dvm *= 0.5;
|
|
}
|
|
if (v_here < dvs2) {
|
|
dvm *= 0.5;
|
|
}
|
|
double dtm = 0.1*t_here;
|
|
double dva = fabs(dv);
|
|
double dta = fabs(dt);
|
|
if (dva > dvm) {
|
|
dv *= dvm/dva;
|
|
}
|
|
if (dta > dtm) {
|
|
dt *= dtm/dta;
|
|
}
|
|
v_here += dv;
|
|
t_here += dt;
|
|
t_here = clip(t_here, Tmin(), Tmax());
|
|
if (v_here <= 0.0) {
|
|
v_here = 0.0001;
|
|
}
|
|
Set(PropertyPair::TV, t_here, v_here);
|
|
LoopCount++;
|
|
if (LoopCount > 200) {
|
|
std::string msg = fmt::format("No convergence. {} = {}, {} = {}",
|
|
propertySymbols[ifx], X, propertySymbols[ify], Y);
|
|
if (t_here == Tmin()) {
|
|
msg += fmt::format("\nAt temperature limit (Tmin = {})", Tmin());
|
|
} else if (t_here == Tmax()) {
|
|
msg += fmt::format("\nAt temperature limit (Tmax = {})", Tmax());
|
|
}
|
|
throw CanteraError("Substance::set_xy", msg);
|
|
}
|
|
}
|
|
}
|
|
|
|
double Substance::prop(propertyFlag::type ijob)
|
|
{
|
|
if (ijob == propertyFlag::P) {
|
|
return P();
|
|
}
|
|
if (ijob == propertyFlag::T) {
|
|
return T;
|
|
}
|
|
double xx = x();
|
|
if ((xx > 0.0) && (xx < 1.0)) {
|
|
double Rho_save = Rho;
|
|
Rho = Rhv;
|
|
double vp = vprop(ijob);
|
|
Rho = Rhf;
|
|
double lp = vprop(ijob);
|
|
double pp = (1.0 - xx)*lp + xx*vp;
|
|
Rho = Rho_save;
|
|
return pp;
|
|
} else {
|
|
return vprop(ijob);
|
|
}
|
|
}
|
|
|
|
static const double ErrP = 1.e-7;
|
|
static const double Big = 1.e30;
|
|
|
|
void Substance::BracketSlope(double Pressure)
|
|
{
|
|
if (kbr == 0) {
|
|
dv = (v_here < Vcrit() ? -0.05*v_here : 0.2*v_here);
|
|
if (Vmin > 0.0) {
|
|
dv = 0.2*v_here;
|
|
}
|
|
if (Vmax < Big) {
|
|
dv = -0.05*v_here;
|
|
}
|
|
} else {
|
|
double dpdv = (Pmax - Pmin)/(Vmax - Vmin);
|
|
v_here = Vmax;
|
|
P_here = Pmax;
|
|
dv = dvbf*(Pressure - P_here)/dpdv;
|
|
dvbf = 0.5*dvbf;
|
|
}
|
|
}
|
|
|
|
void Substance::set_TPp(double Temp, double Pressure)
|
|
{
|
|
kbr = 0;
|
|
dvbf = 1.0;
|
|
Vmin = 0.0;
|
|
Vmax = Big;
|
|
Pmin = Big;
|
|
Pmax = 0.0;
|
|
double dvs1 = 2.0*Vcrit();
|
|
double dvs2 = 0.7*Vcrit();
|
|
int LoopCount = 0;
|
|
|
|
double v_save = 1.0/Rho;
|
|
T = Temp;
|
|
v_here = vp();
|
|
|
|
// loop
|
|
while (P_here = Pp(),
|
|
fabs(Pressure - P_here) >= ErrP* Pressure || LoopCount == 0) {
|
|
if (P_here < 0.0) {
|
|
BracketSlope(Pressure);
|
|
} else {
|
|
dv = 0.001*v_here;
|
|
if (v_here <= Vcrit()) {
|
|
dv *= -1.0;
|
|
}
|
|
Set(PropertyPair::TV, Temp, v_here+dv);
|
|
double dpdv = (Pp() - P_here)/dv;
|
|
if (dpdv > 0.0) {
|
|
BracketSlope(Pressure);
|
|
} else {
|
|
if ((P_here > Pressure) && (v_here > Vmin)) {
|
|
Vmin = v_here;
|
|
} else if ((P_here < Pressure) && (v_here < Vmax)) {
|
|
Vmax = v_here;
|
|
}
|
|
if (v_here == Vmin) {
|
|
Pmin = P_here;
|
|
}
|
|
if (v_here == Vmax) {
|
|
Pmax = P_here;
|
|
}
|
|
if (Vmin >= Vmax) {
|
|
throw CanteraError("Substance::set_TPp","Vmin >= Vmax");
|
|
} else if ((Vmin > 0.0) && (Vmax < Big)) {
|
|
kbr = 1;
|
|
}
|
|
dvbf = 1.0;
|
|
if (dpdv == 0.0) {
|
|
dvbf = 0.5;
|
|
BracketSlope(Pressure);
|
|
} else {
|
|
dv = (Pressure - P_here)/dpdv;
|
|
}
|
|
}
|
|
}
|
|
double dvm = 0.2*v_here;
|
|
if (v_here < dvs1) {
|
|
dvm *= 0.5;
|
|
}
|
|
if (v_here < dvs2) {
|
|
dvm *= 0.5;
|
|
}
|
|
if (kbr != 0) {
|
|
double vt = v_here + dv;
|
|
if ((vt < Vmin) || (vt > Vmax)) {
|
|
dv = Vmin + (Pressure - Pmin)*(Vmax - Vmin)/(Pmax - Pmin) - v_here;
|
|
}
|
|
}
|
|
double dva = fabs(dv);
|
|
if (dva > dvm) {
|
|
dv *= dvm/dva;
|
|
}
|
|
v_here += dv;
|
|
if (dv == 0.0) {
|
|
throw CanteraError("Substance::set_TPp","dv = 0 and no convergence");
|
|
}
|
|
Set(PropertyPair::TV, Temp, v_here);
|
|
LoopCount++;
|
|
if (LoopCount > 100) {
|
|
Set(PropertyPair::TV, Temp, v_save);
|
|
throw CanteraError("Substance::set_TPp",
|
|
"no convergence for P* = {}, V* = {}",
|
|
Pressure/Pcrit(), v_save/Vcrit());
|
|
}
|
|
}
|
|
Set(PropertyPair::TV, Temp,v_here);
|
|
}
|
|
}
|