int freesteam_region_pv(double p, double v){
double p13 = freesteam_region4_psat_T(REGION1_TMAX);
if(p > p13){
double v13 = freesteam_region1_v_pT(p, REGION1_TMAX);
if(v < v13) return 1;
/* region 2-3 */
double T23 = freesteam_b23_T_p(p);
double v23 = freesteam_region2_v_pT(p,T23);
if(v > v23) return 2;
/* region 3? or high-pressure part of region 4? */
if(p >= IAPWS97_PCRIT) return 3;
double Tsat = freesteam_region4_Tsat_p(p);
double vf = 1./ freesteam_region4_rhof_T(Tsat);
if(v < vf) return 3;
double vg = 1./ freesteam_region4_rhog_T(Tsat);
if(v > vg) return 3;
return 4;
}else{
double Tsat = freesteam_region4_Tsat_p(p);
double vf = freesteam_region1_v_pT(p,Tsat);
if(v < vf) return 1;
double vg = freesteam_region2_v_pT(p,Tsat);
if(v > vg) return 2;
return 4;
}
}
int freesteam_region_pu(double p, double u){
double p13 = freesteam_region4_psat_T(REGION1_TMAX);
if(p < p13){
double Tsat = freesteam_region4_Tsat_p(p);
double uf = freesteam_region1_u_pT(p,Tsat);
if(u < uf)return 1;
double ug = freesteam_region2_u_pT(p,Tsat);
if(u > ug)return 2;
return 4;
}
double u13 = freesteam_region1_u_pT(p,REGION1_TMAX);
if(u < u13){
return 1;
}
double T23 = freesteam_b23_T_p(p);
double u23 = freesteam_region2_u_pT(p,T23);
if(u > u23){
return 2;
}
if(p > IAPWS97_PCRIT)return 3;
/* FIXME what we really need here is a psat(u) function! The current method
is singular. */
double Tsat = freesteam_region4_Tsat_p(p);
double rhof = freesteam_region4_rhof_T(Tsat);
double uf = freesteam_region3_u_rhoT(rhof,Tsat);
if(u<uf) return 3;
double rhog = freesteam_region4_rhog_T(Tsat);
double ug = freesteam_region3_u_rhoT(rhog,Tsat);
if(u>ug)return 3;
return 4;
}
/**
This function will never return region 4, because it's not possible
to 'sit on the knife' of saturation. If you need to set saturated states,
you should use another function such as freesteam_region1_set_Tx.
*/
SteamState freesteam_set_pT(double p, double T){
SteamState S;
if(T < REGION1_TMAX){
if(p > freesteam_region4_psat_T(T)){
S.region = 1;
S.R1.T = T;
S.R1.p = p;
}else{
S.region = 2;
S.R2.T = T;
S.R2.p = p;
}
}else{
//fprintf(stderr,"%s: T = %g >= REGION1_TMAX = %g\n",__func__,T,REGION1_TMAX);
/* FIXME some optimisation possiblxe here with test for lower pressures */
double T23 = freesteam_b23_T_p(p);
double p23min = freesteam_b23_p_T(REGION1_TMAX);
if(p < p23min || T > T23){
//fprintf(stderr,"%s: T = %g > T23 = %g\n",__func__,T,T23);
S.region = 2;
S.R2.T = T;
S.R2.p = p;
}else{
/* FIXME the limit values are all wrong here! */
//fprintf(stderr,"%s: region 3\n",__func__);
SteamPTData D = {p,T};
double ub = 1./freesteam_region1_v_pT(IAPWS97_PMAX,REGION1_TMAX);
double lb = 1./freesteam_region2_v_pT(freesteam_b23_p_T(T),T);
/* if we're in the little wee area around the critical pt... */
if(T < IAPWS97_TCRIT){
double psat = freesteam_region4_psat_T(T);
if(p < psat){
ub = freesteam_region4_rhog_T(T);
assert(lb<ub);
}else{
lb = freesteam_region4_rhof_T(T);
//fprintf(stderr,"lb = %g, ub = %g\n",lb,ub);
assert(lb<ub);
}
}
double tol = 1e-7;
double sol, err = 0;
if(zeroin_solve(&pT_region3_fn, &D, lb, ub, tol, &sol, &err)){
fprintf(stderr,"%s (%s:%d): failed to solve for rho\n",__func__,__FILE__,__LINE__);
exit(1);
}
S.region = 3;
S.R3.T = T;
S.R3.rho = sol;
//assert(fabs((freesteam_p(S) - p)/p) < tol);
}
}
//fprintf(stderr,"%s: region %d\n",__func__,S.region);
return S;
}
double freesteam_region4_v_Tx(double T, double x){
double vf, vg;
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
vf = freesteam_region1_v_pT(psat,T);
vg = freesteam_region2_v_pT(psat,T);
}else{
vf = 1./ freesteam_region4_rhof_T(T);
vg = 1./ freesteam_region4_rhog_T(T);
}
return vf + x*(vg - vf);
}
/**
This function will always return saturated mixtures; no negative or >1
values of x are being 'understood' here (although one can give them meaning
based on extrapolated values of u or h of v, for example...)
*/
SteamState freesteam_set_Tx(double T, double x) {
SteamState S;
if(T >= IAPWS97_TCRIT) {
/* region 3 supercritical. just return a state with the specified
temperature and the critical point entropy. arbitrary. */
SolveTSData D = {T, freesteam_region3_s_rhoT(IAPWS97_RHOCRIT, IAPWS97_TCRIT)};
double ub = 1./freesteam_region1_v_pT(IAPWS97_PMAX,REGION1_TMAX);
double lb = 1./freesteam_region2_v_pT(freesteam_b23_p_T(T),T);
double tol = 1e-7;
double sol, err = 0;
if(zeroin_solve(&Ts_region3_fn, &D, lb, ub, tol, &sol, &err)) {
fprintf(stderr,"%s (%s:%d): failed to solve for rho\n",__func__,__FILE__,__LINE__);
exit(1);
}
S.region = 3;
S.R3.T = T;
S.R3.rho = sol;
} else if(x <= 0) {
if(T > REGION1_TMAX) {
S.region = 3;
S.R3.T = T;
S.R3.rho = freesteam_region4_rhof_T(T);
/* FIXME iteratively refine the value */
} else {
S.region = 1;
S.R1.p = freesteam_region4_psat_T(T);
S.R1.T = T;
}
} else if(x >= 1) {
if(T > REGION1_TMAX) {
S.region = 3;
S.R3.T = T;
S.R3.rho = freesteam_region4_rhog_T(T);
/* FIXME iteratively refine the value */
} else {
S.region = 2;
S.R1.p = freesteam_region4_psat_T(T);
S.R1.T = T;
}
} else {
/* finally! */
S.region = 4;
S.R4.T = T;
S.R4.x = x;
}
return S;
}
double freesteam_drhogdT_T(double T){
double dpsatdT = freesteam_region4_dpsatdT_T(T);
double rhog = freesteam_region4_rhog_T(T);
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
SteamState Sg = freesteam_region2_set_pT(psat,T);
double vf = freesteam_v(Sg);
return -1./SQ(vf) * (PT2('v',Sg) * dpsatdT + TP2('v',Sg));
}else{
SteamState Sg = freesteam_region3_set_rhoT(rhog,T);
double dpdT = TV3('p',Sg);
double dpdrho = -1./SQ(rhog) * VT3('p',Sg);
return (dpsatdT - dpdT)/dpdrho;
}
}
double freesteam_region4_cv_Tx(double T, double x){
double cvf, cvg;
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
cvf = freesteam_region1_cv_pT(psat,T);
cvg = freesteam_region2_cv_pT(psat,T);
}else{
double rhof, rhog;
rhof = freesteam_region4_rhof_T(T);
rhog = freesteam_region4_rhog_T(T);
cvf = freesteam_region3_cv_rhoT(rhof,T);
cvg = freesteam_region3_cv_rhoT(rhog,T);
}
return cvf + x*(cvg - cvf);
}
double freesteam_region4_cp_Tx(double T, double x){
double cpf, cpg;
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
cpf = freesteam_region1_cp_pT(psat,T);
cpg = freesteam_region2_cp_pT(psat,T);
}else{
double rhof, rhog;
rhof = freesteam_region4_rhof_T(T);
rhog = freesteam_region4_rhog_T(T);
cpf = freesteam_region3_cp_rhoT(rhof,T);
cpg = freesteam_region3_cp_rhoT(rhog,T);
}
return cpf + x*(cpg - cpf);
}
double freesteam_region4_s_Tx(double T, double x){
double sf, sg;
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
sf = freesteam_region1_s_pT(psat,T);
sg = freesteam_region2_s_pT(psat,T);
}else{
double rhof, rhog;
rhof = freesteam_region4_rhof_T(T);
rhog = freesteam_region4_rhog_T(T);
sf = freesteam_region3_s_rhoT(rhof,T);
sg = freesteam_region3_s_rhoT(rhog,T);
}
return sf + x*(sg - sf);
}
double freesteam_region4_u_Tx(double T, double x){
double uf, ug;
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
uf = freesteam_region1_u_pT(psat,T);
ug = freesteam_region2_u_pT(psat,T);
}else{
double rhof, rhog;
rhof = freesteam_region4_rhof_T(T);
rhog = freesteam_region4_rhog_T(T);
uf = freesteam_region3_u_rhoT(rhof,T);
ug = freesteam_region3_u_rhoT(rhog,T);
}
return uf + x*(ug - uf);
}
double freesteam_region4_h_Tx(double T, double x){
double hf, hg;
if(T < REGION1_TMAX){
double psat = freesteam_region4_psat_T(T);
hf = freesteam_region1_h_pT(psat,T);
hg = freesteam_region2_h_pT(psat,T);
//fprintf(stderr,"%s: T = %f K, psat = %f MPa, hf = %f kJ/kg, hg = %f kJ/kg\n",__func__,T,psat/1e6,hf/1e3,hg);
}else{
double rhof, rhog;
rhof = freesteam_region4_rhof_T(T);
rhog = freesteam_region4_rhog_T(T);
hf = freesteam_region3_h_rhoT(rhof,T);
hg = freesteam_region3_h_rhoT(rhog,T);
}
return hf + x*(hg - hf);
}
/*
⎰ ∂z ⎱ = ⎰∂z_f⎱ (1 - x) + ⎰∂z_f⎱ x
⎱ ∂T ⎰x ⎱ ∂T ⎰ ⎱ ∂T ⎰
*/
double freesteam_region4_dAdTx(FREESTEAM_CHAR z, SteamState S){
double res;
#define T S.R4.T
switch(z){
case 'p': res = freesteam_region4_dpsatdT_T(T); return res;
case 'T': res = 1; return res;
case 'x': res = 0; return res;
}
//fprintf(stderr,"%s: T = %g\n",__func__,T);
assert(!isnan(T));
double dzfdT, dzgdT;
if(T < REGION1_TMAX){
//fprintf(stderr,"%s: below REGION1_TMAX\n",__func__);
double psat = freesteam_region4_psat_T(T);
SteamState Sf = freesteam_region1_set_pT(psat,T);
SteamState Sg = freesteam_region2_set_pT(psat,T);
double dpsatdT = freesteam_region4_dpsatdT_T(T);
dzfdT = PT1(z,Sf)*dpsatdT + TP1(z,Sf);
dzgdT = PT2(z,Sg)*dpsatdT + TP2(z,Sg);
}else{
double rhof = freesteam_region4_rhof_T(T);
double rhog = freesteam_region4_rhog_T(T);
assert(rhof!=0);
assert(rhog!=0);
SteamState Sf = freesteam_region3_set_rhoT(rhof,T);
SteamState Sg = freesteam_region3_set_rhoT(rhog,T);
double dvfdT = -1./SQ(rhof) * freesteam_drhofdT_T(T);
assert(!isnan(dvfdT));
double dvgdT = -1./SQ(rhog) * freesteam_drhogdT_T(T);
assert(!isnan(dvgdT));
dzfdT = VT3(z,Sf)*dvfdT + TV3(z,Sf);
dzgdT = VT3(z,Sg)*dvgdT + TV3(z,Sg);
}
assert(!isnan(dzfdT));
assert(!isnan(dzgdT));
#define x S.R4.x
res = dzfdT*(1-x) + dzgdT*x;
//fprintf(stderr,"(∂%c/∂T)x = %g\n",z,res);
return res;
#undef T
#undef x
}
SteamState freesteam_set_pv(double p, double v){
SteamState S;
S.region = (char)freesteam_region_pv(p,v);
#if 0
int status;
#endif
switch(S.region){
case 1:
/* iterate T to get correct value of v */
S.R1.p = p;
S.R1.T = freesteam_region4_Tsat_p(p);
{
double lb = IAPWS97_TMIN;
double ub = REGION1_TMAX;
double tol = 1e-9; /* ??? */
double sol, err;
SolvePVData D = {p, v};
zeroin_solve(&pv_region1_fn, &D, lb, ub, tol, &sol, &err);
S.R1.T = sol;
/* FIXME check convergence! */
}
#if 0
S = freesteam_solver2_region1('p','v', p, v, S, &status);
if(status){
fprintf(stderr,"%s: WARNING: Failed to converge in region 1\n",__func__);
}
#endif
break;
case 2:
/* iterate T to get correct value of v */
S.R2.p = p;
S.R2.T = freesteam_region4_Tsat_p(p);
{
double lb = IAPWS97_TMIN;
double ub = IAPWS97_TMAX;
double tol = 1e-9; /* ??? */
double sol, err;
SolvePVData D = {p, v};
zeroin_solve(&pv_region2_fn, &D, lb, ub, tol, &sol, &err);
S.R2.T = sol;
/* FIXME check convergence! */
}
#if 0
S.R2.p = p;
S.R2.T = freesteam_region4_Tsat_p(p);
S = freesteam_solver2_region2('p','v', p, v, S, &status);
if(status){
fprintf(stderr,"%s: WARNING: Failed to converge in region 2\n",__func__);
}
#endif
break;
case 3:
S.R3.rho = 1./ v;
S.R3.T = REGION1_TMAX;
{
double lb = REGION1_TMAX;
double ub = IAPWS97_TMAX;
double tol = 1e-12; /* ??? */
double sol, err;
SolvePRhoData D = {p, S.R3.rho};
zeroin_solve(&pv_region3_fn, &D, lb, ub, tol, &sol, &err);
S.R3.T = sol;
//fprintf(stderr,"%s: (p = %f MPa,v = %f m3/kg) region 3, error in p = %f\n",__func__,p,v, err);
/* FIXME check convergence! */
}
#if 0
S = freesteam_solver2_region3('p','v', p, v, S, &status);
if(status){
fprintf(stderr,"%s: WARNING: Failed to converge in region 3\n",__func__);
}
#endif
break;
case 4:
S.R4.T = freesteam_region4_Tsat_p(p);
//fprintf(stderr,"%s: region 4, Tsat = %g\n",__func__,S.R4.T);
double vf, vg;
if(S.R4.T <= REGION1_TMAX){
vf = freesteam_region1_v_pT(p,S.R4.T);
vg = freesteam_region2_v_pT(p,S.R4.T);
}else{
/* TODO iteratively improve estimate of T */
vf = 1./ freesteam_region4_rhof_T(S.R4.T);
vg = 1./ freesteam_region4_rhog_T(S.R4.T);
}
S.R4.x = (v - vf)/(vg - vf);
}
return S;
}
//CL: drhodh=(drho/dh)_p=const
Foam::scalar Foam::drhodh(SteamState S)
{
label region;
scalar cp,beta,drhodh,rho;
region=freesteam_region(S);
if (region==1)
{
rho=1/freesteam_region1_v_pT(S.R1.p,S.R1.T);
//Cl: note: in FreeStream, beta=1/V*(dV/dP)_P=const is called alphaV (in this region)
beta=freesteam_region1_alphav_pT(S.R1.p,S.R1.T);
cp=freesteam_region1_cp_pT(S.R1.p,S.R1.T);
//CL: getting derivatives using Bridgmans table
//CL: drhodh=(drho/dh)_p=const
drhodh=-rho*beta/cp;
}
else if (region==2)
{
rho=1/freesteam_region2_v_pT(S.R2.p,S.R2.T);
//Cl: note: in FreeStream, beta=1/V*(dV/dP)_P=const is called alphaV (in this region)
//Cl: note: in FreeStream, kappa=1/V*(dV/dP)_T=const is called kappaT (in this region)
beta=freesteam_region2_alphav_pT(S.R2.p,S.R2.T);
cp=freesteam_region2_cp_pT(S.R2.p,S.R2.T);
//CL: getting derivatives using Bridgmans table
//CL: drhodh=(drho/dh)_p=const
drhodh=-rho*beta/cp;
}
else if (region==3)
{
scalar gamma,cv,p;
p=freesteam_region3_p_rhoT(S.R3.rho,S.R3.T);
//Cl: note: beta=1/V*(dV/dP)_P=const
//Cl: note: in FreeStream, gamma=1/p*(dp/dT)_v=const is called alphap (in this region
gamma=freesteam_region3_alphap_rhoT(S.R3.rho,S.R3.T);
cp=freesteam_region3_cp_rhoT(S.R3.rho,S.R3.T);
cv=freesteam_region3_cv_rhoT(S.R3.rho,S.R3.T);
beta=(cp-cv)/(S.R3.T/S.R3.rho*p*gamma);
//CL: getting derivatives using Bridgmans table
//CL: drhodh=(drho/dh)_p=const
drhodh=-S.R3.rho*beta/cp;
}
else if (region==4)
{
scalar vv,vl,hl,hv,p;
SteamState Sl,Sv;
rho=1/freesteam_region4_v_Tx(S.R4.T,S.R4.x);
p=freesteam_region4_psat_T(S.R4.T);
//CL: Getting density on the vapour and liquid lines
vv=1/freesteam_region4_rhog_T(S.R4.T);
vl=1/freesteam_region4_rhof_T(S.R4.T);
// getting the states outside the vapour dome
Sl=freesteam_set_pv(p,vl-0.0000001); //inside region 1
Sv=freesteam_set_pv(p,vv+0.0000001); //inside region 2
hl=freesteam_region1_h_pT(Sl.R1.p,Sl.R1.T);
hv=freesteam_region2_h_pT(Sv.R2.p,Sv.R2.T);
//CL: drhodh=(drho/dh)_p=const
drhodh=-rho*rho*(vv-vl)/(hv-hl);
}
else
{
Info<<"IAPWS-IF97.C error, outside the regions 1-4"<<endl;
}
return drhodh;
}
//CL: psiH=(drho/dp)_h=const
Foam::scalar Foam::psiH(SteamState S)
{
label region;
scalar kappa,cp,beta,psiH,rho;
region=freesteam_region(S);
if (region==1)
{
//Cl: note: in FreeStream, beta=1/V*(dV/dP)_P=const is called alphaV (in this region)
//Cl: note: in FreeStream, kappa=1/V*(dV/dP)_T=const is called kappaT (in this region)
kappa=freesteam_region1_kappaT_pT(S.R1.p,S.R1.T);
beta=freesteam_region1_alphav_pT(S.R1.p,S.R1.T);
cp=freesteam_region1_cp_pT(S.R1.p,S.R1.T);
rho=1/freesteam_region1_v_pT(S.R1.p,S.R1.T);
//CL: getting derivatives using Bridgmans table
//CL: psiH=(drho/dp)_h=const
psiH=-((S.R1.T*beta*beta-beta)/cp-kappa*rho);
}
else if (region==2)
{
//Cl: note: in FreeStream, beta=1/V*(dV/dP)_P=const is called alphaV (in this region)
//Cl: note: in FreeStream, kappa=1/V*(dV/dP)_T=const is called kappaT (in this region)
kappa=freesteam_region2_kappaT_pT(S.R2.p,S.R2.T);
beta=freesteam_region2_alphav_pT(S.R2.p,S.R2.T);
cp=freesteam_region2_cp_pT(S.R2.p,S.R2.T);
rho=1/freesteam_region2_v_pT(S.R2.p,S.R2.T);
//CL: getting derivatives using Bridgmans table
//CL: psiH=(drho/dp)_h=const
psiH=-((S.R2.T*beta*beta-beta)/cp-kappa*rho);
}
else if (region==3)
{
scalar gamma,cv,p;
rho=S.R3.rho;
p=freesteam_region3_p_rhoT(S.R3.rho,S.R3.T);
//Cl: note: beta=1/V*(dV/dP)_P=const
//Cl: note: kappa=1/V*(dV/dP)_T=const
//Cl: note: in FreeStream, gamma=1/p*(dp/dT)_v=const is called alphap (in this region
gamma=freesteam_region3_alphap_rhoT(S.R3.rho,S.R3.T);
cp=freesteam_region3_cp_rhoT(S.R3.rho,S.R3.T);
cv=freesteam_region3_cv_rhoT(S.R3.rho,S.R3.T);
beta=(cp-cv)/(S.R3.T/S.R3.rho*p*gamma);
kappa=(cp-cv)/(S.R3.T/S.R3.rho*p*p*gamma*gamma);
//CL: getting derivatives using Bridgmans table
//CL: psiH=(drho/dp)_h=const
psiH=-((S.R3.T*beta*beta-beta)/cp-kappa*rho);
}
else if (region==4)
{
scalar rhov,rhol,betav,betal,kappav,kappal,vv,vl,cpl,cpv,hl,hv,h,p;
scalar dvldp,dvvdp,dhldp,dhvdp;
scalar dpdT,dvdp,dxdp;
SteamState Sl,Sv;
rho=1/freesteam_region4_v_Tx(S.R4.T,S.R4.x);
h=freesteam_region4_h_Tx(S.R4.T,S.R4.x);
p=freesteam_region4_psat_T(S.R4.T);
//CL: Getting density on the vapour and liquid lines
rhov=freesteam_region4_rhog_T(S.R4.T);
rhol=freesteam_region4_rhof_T(S.R4.T);
vv=1/rhov;
vl=1/rhol;
//CL: getting derivatives --> this is a bit tricky in the vapor dome
dpdT=freesteam_region4_dpsatdT_T(S.R4.T);
// getting the states outside the vapour dome
Sl=freesteam_set_pv(p,vl-0.0000001); //inside region 1
Sv=freesteam_set_pv(p,vv+0.0000001); //inside region 2
kappal=freesteam_region1_kappaT_pT(Sl.R1.p,Sl.R1.T);
kappav=freesteam_region2_kappaT_pT(Sv.R2.p,Sv.R2.T);
betal=freesteam_region1_alphav_pT(Sl.R1.p,Sl.R1.T);
betav=freesteam_region2_alphav_pT(Sv.R2.p,Sv.R2.T);
cpl=freesteam_region1_cp_pT(Sl.R1.p,Sl.R1.T);
cpv=freesteam_region2_cp_pT(Sv.R2.p,Sv.R2.T);
hl=freesteam_region1_h_pT(Sl.R1.p,Sl.R1.T);
hv=freesteam_region2_h_pT(Sv.R2.p,Sv.R2.T);
//calculation derviatives on liquid and vapour line
dvldp=betal*vl/dpdT-kappal*vl;
dvvdp=betav*vv/dpdT-kappav*vv;
dhldp=vl*(1-betal*Sl.R1.T)+cpl/dpdT;
dhvdp=vv*(1-betav*Sv.R2.T)+cpl/dpdT;
dxdp=-dhldp/(hv-hl)
+(h-hl)/((hv-hl)*(hv-hl))
*(dhvdp-dhldp);
//CL: psiH=(drho/dp)_h=const
dvdp=dvldp+(dvvdp-dvldp)*S.R4.x+(vv-vl)*dxdp;
psiH=-rho*rho*dvdp;
}
else
{
Info<<"IAPWS-IF97.C error, outside the regions 1-4"<<endl;
}
return psiH;
}
//CL: calculated the properties --> this function is called by the functions above
//CL: does not calulated the internal energy, if this is needed e.g. for sonicFoam
//CL: the function has to be changed a little bit
void Foam::calculateProperties_h
(
SteamState S,
scalar &p,
scalar &h,
scalar &T,
scalar &rho,
scalar &psi,
scalar &drhodh,
scalar &mu,
scalar &alpha,
scalar &x
)
{
label region;
scalar kappa,lambda,cp,beta;
region=freesteam_region(S);
if (region==1)
{
p=S.R1.p;
T=S.R1.T;
rho=1/freesteam_region1_v_pT(S.R1.p,S.R1.T);
h=freesteam_region1_h_pT(S.R1.p,S.R1.T);
x=0;
//Cl: note: in FreeStream, beta=1/V*(dV/dP)_P=const is called alphaV (in this region)
//Cl: note: in FreeStream, kappa=1/V*(dV/dP)_T=const is called kappaT (in this region)
kappa=freesteam_region1_kappaT_pT(S.R1.p,S.R1.T);
beta=freesteam_region1_alphav_pT(S.R1.p,S.R1.T);
cp=freesteam_region1_cp_pT(S.R1.p,S.R1.T);
//CL: getting derivatives using Bridgmans table
//CL: psi=(drho/dp)_h=const
//CL: drhodh=(drho/dh)_p=const
psi=-((T*beta*beta-beta)/cp-kappa*rho);
drhodh=-rho*beta/cp;
//CL: getting transport properties
mu=freesteam_mu_rhoT(rho, T);
lambda=freesteam_k_rhoT(rho,T);
alpha=lambda/cp; //Cl: Important info -->alpha= thermal diffusivity time density
}
else if (region==2)
{
p=S.R2.p;
T=S.R2.T;
rho=1/freesteam_region2_v_pT(S.R2.p,S.R2.T);
h=freesteam_region2_h_pT(S.R2.p,S.R2.T);
x=1;
//Cl: note: in FreeStream, beta=1/V*(dV/dP)_P=const is called alphaV (in this region)
//Cl: note: in FreeStream, kappa=1/V*(dV/dP)_T=const is called kappaT (in this region)
kappa=freesteam_region2_kappaT_pT(S.R2.p,S.R2.T);
beta=freesteam_region2_alphav_pT(S.R2.p,S.R2.T);
cp=freesteam_region2_cp_pT(S.R2.p,S.R2.T);
//CL: getting derivatives using Bridgmans table
//CL: psi=(drho/dp)_h=const
//CL: drhodh=(drho/dh)_p=const
psi=-((T*beta*beta-beta)/cp-kappa*rho);
drhodh=-rho*beta/cp;
//CL: getting transport properties
mu=freesteam_mu_rhoT(rho, T);
lambda=freesteam_k_rhoT(rho,T);
alpha=lambda/cp; //Cl: Important info -->alpha= thermal diffusivity time density
}
else if (region==3)
{
scalar gamma,cv;
rho=S.R3.rho;
T=S.R3.T;
p=freesteam_region3_p_rhoT(S.R3.rho,S.R3.T);
h=freesteam_region3_h_rhoT(S.R3.rho,S.R3.T);
//CL= when h<h @ critical point -->x=0 else x=1
if (h<2084256.263)
{
x=0;
}
else
{
x=1;
}
//Cl: note: beta=1/V*(dV/dP)_P=const
//Cl: note: kappa=1/V*(dV/dP)_T=const
//Cl: note: in FreeStream, gamma=1/p*(dp/dT)_v=const is called alphap (in this region)
gamma=freesteam_region3_alphap_rhoT(S.R3.rho,S.R3.T);
cp=freesteam_region3_cp_rhoT(S.R3.rho,S.R3.T);
cv=freesteam_region3_cv_rhoT(S.R3.rho,S.R3.T);
beta=(cp-cv)/(S.R3.T/S.R3.rho*p*gamma);
kappa=(cp-cv)/(S.R3.T/S.R3.rho*p*p*gamma*gamma);
//CL: getting derivatives using Bridgmans table
//CL: psi=(drho/dp)_h=const
//CL: drhodh=(drho/dh)_p=const
psi=-((T*beta*beta-beta)/cp-kappa*rho);
drhodh=-rho*beta/cp;
//CL: getting transport properties
mu=freesteam_mu_rhoT(rho, T);
lambda=freesteam_k_rhoT(rho,T);
alpha=lambda/cp; //Cl: Important info -->alpha= thermal diffusivity time density
}
else if (region==4)
{
scalar rhov,rhol,betav,betal,kappav,kappal,vv,vl,cpl,cpv,hl,hv,cp;
scalar dvldp,dvvdp,dhldp,dhvdp;
scalar dpdT,dvdh,dvdp,dxdp;
SteamState Sl,Sv;
x=S.R4.x;
T=S.R4.T;
rho=1/freesteam_region4_v_Tx(S.R4.T,S.R4.x);
h=freesteam_region4_h_Tx(S.R4.T,S.R4.x);
p=freesteam_region4_psat_T(S.R4.T);
cp=freesteam_region4_cp_Tx(S.R4.T,S.R4.x);
//CL: Getting density on the vapour and liquid lines
rhov=freesteam_region4_rhog_T(S.R4.T);
rhol=freesteam_region4_rhof_T(S.R4.T);
vv=1/rhov;
vl=1/rhol;
//CL: getting derivatives --> this is a bit tricky inside the vapor dome
dpdT=freesteam_region4_dpsatdT_T(S.R4.T);
// getting the states outside the vapour dome
Sl=freesteam_set_pv(p,vl-0.0000001); //inside region 1
Sv=freesteam_set_pv(p,vv+0.0000001); //inside region 2
kappal=freesteam_region1_kappaT_pT(Sl.R1.p,Sl.R1.T);
kappav=freesteam_region2_kappaT_pT(Sv.R2.p,Sv.R2.T);
betal=freesteam_region1_alphav_pT(Sl.R1.p,Sl.R1.T);
betav=freesteam_region2_alphav_pT(Sv.R2.p,Sv.R2.T);
cpl=freesteam_region1_cp_pT(Sl.R1.p,Sl.R1.T);
cpv=freesteam_region2_cp_pT(Sv.R2.p,Sv.R2.T);
hl=freesteam_region1_h_pT(Sl.R1.p,Sl.R1.T);
hv=freesteam_region2_h_pT(Sv.R2.p,Sv.R2.T);
//calculation derviatives on liquid and vapour line
dvldp=betal*vl/dpdT-kappal*vl;
dvvdp=betav*vv/dpdT-kappav*vv;
dhldp=vl*(1-betal*Sl.R1.T)+cpl/dpdT;
dhvdp=vv*(1-betav*Sv.R2.T)+cpl/dpdT;
dxdp=-dhldp/(hv-hl)
+(h-hl)/((hv-hl)*(hv-hl))
*(dhvdp-dhldp);
//CL: psi=(drho/dp)_h=const
dvdp=dvldp+(dvvdp-dvldp)*x+(vv-vl)*dxdp;
psi=-rho*rho*dvdp;
//CL: drhodh=(drho/dh)_p=const
dvdh=(vv-vl)/(hv-hl);
drhodh=-rho*rho*dvdh;
//CL: getting transport properties
mu=freesteam_mu_rhoT(rho, T);
lambda=freesteam_k_rhoT(rho,T);
alpha=lambda/cp; //Cl: Important info -->alpha= thermal diffusivity time density
}
else
{
std::cout<<"IAPWS-IF97 error, outside the regions 1-4"<<std::endl;
}
}