public static RefHTCandDPResult HTCandDP(string[] fluid, double[] composition, double d, double g, double p, double x, double l, double q, double zh, double zdp)
{
//Main function for 2-phase flow HTC and calculation
double href = 0;
double PressD = 0;
//*************Smoothening HTC & DP at single-to-2 phase transitions****************
//********divided to 2 region based on quality (0 - 0.95 - 1) to calculated HTC & DP********
if (x <= 0.95 && x >= 0)
{
href = RefrigerantTPHTC.Shah_Evap_href(fluid, composition, d, g, p, x, q, l);
PressD = RefrigerantTPDP.deltap_smooth(fluid, composition, d, g, p, x, l);
}
if (x < 1 && x > 0.95) //vapor to 2-phase
{
href = RefrigerantTPHTC.Shah_Evap_href(fluid, composition, d, g, p, 0.95, q, l);
PressD = RefrigerantTPDP.deltap_smooth(fluid, composition, d, g, p, 0.95, l);
}
//********divided to 4 region based on quality (0 - 0.05 - 0.9 - 0.95 - 1) to calculated HTC & DP END********
href = href * zh;
PressD = PressD * zdp;
return(new RefHTCandDPResult {
Href = href, DPref = PressD
});
}
public static RefHTCandDPResult HTCandDP_2p(string fluid, double d, double g, double p, double x, double l, double q, double zh, double zdp, double hexType, AbstractState coolprop)
{
//Main function for 2-phase flow HTC and calculation
double href = 0;
double PressD = 0;
//********Smoothening HTC & DP at single-to-2 phase transitions********"
//Use lambda to avoid discontinutities of the two phase-liquid and vapor-two-phase and liquid"
double x_transition;
double lambdaL = 0;
double lambdaV = 0;
double h_ref_2phase, deltap_2phase;
double beta = 50; //"Controlling factor for the sharpness of the transition"
RefHTCandDPResult htc_dp_single_sat = new RefHTCandDPResult();
if (x <= 0.05 && x >= 0)
{
x_transition = 0.05;
lambdaL = (1 + Math.Tanh(beta * (x - x_transition))) / 2;
}
else if (x < 1 && x > 0.9)
{
x_transition = 0.9; //"0.95 for pressure drop"
lambdaV = (1 + Math.Tanh(beta * (x - x_transition))) / 2;
}
//"********Smoothening HTC & DP at single-to-2 phase transitions END********"
//*************Smoothening HTC & DP at single-to-2 phase transitions****************
//********divided to 3 region based on quality (0 - 0.05 - 0.95 - 1) to calculated HTC & DP********
if (hexType == 0)
{
if (x < 0.05 && x > 0)
{
h_ref_2phase = RefrigerantTPHTC.Shah_Evap_href(fluid, d, g, p, x, q, l, coolprop);
//href = RefrigerantTPHTC.Kandlikar_Evap_href(fluid, composition, d, g, p, x, q, l);
//href = RefrigerantTPHTC.JR_Evap_href(fluid, composition, d, g, p, x, q, l);
deltap_2phase = RefrigerantTPDP.deltap_smooth(fluid, d, g, p, x, l, coolprop);
//PressD = RefrigerantTPDP.deltap_JR(fluid, composition, d, g, p, x, l);
//PressD = RefrigerantTPDP.deltap_MS(fluid, composition, d, g, p, x, l);
htc_dp_single_sat = RefrigerantHTCandDP.HTCandDP_1p_sat(fluid, d, g, p, 0, l, coolprop); //x=0
href = (1 - lambdaL) * htc_dp_single_sat.Href + lambdaL * h_ref_2phase;
PressD = (1 - lambdaL) * htc_dp_single_sat.DPref + lambdaL * deltap_2phase;
}
else if (x <= 0.9)
{
href = RefrigerantTPHTC.Shah_Evap_href(fluid, d, g, p, x, q, l, coolprop);
//href = RefrigerantTPHTC.Kandlikar_Evap_href(fluid, composition, d, g, p, x, q, l);
//href = RefrigerantTPHTC.JR_Evap_href(fluid, composition, d, g, p, x, q, l);
PressD = RefrigerantTPDP.deltap_smooth(fluid, d, g, p, x, l, coolprop);
//PressD = RefrigerantTPDP.deltap_JR(fluid, composition, d, g, p, x, l);
//PressD = RefrigerantTPDP.deltap_MS(fluid, composition, d, g, p, x, l);
}
else //vapor to 2-phase
{
h_ref_2phase = RefrigerantTPHTC.Shah_Evap_href(fluid, d, g, p, x, q, l, coolprop);
//href = RefrigerantTPHTC.Kandlikar_Evap_href(fluid, composition, d, g, p, x, q, l);
//href = RefrigerantTPHTC.JR_Evap_href(fluid, composition, d, g, p, x, q, l);
deltap_2phase = RefrigerantTPDP.deltap_smooth(fluid, d, g, p, x, l, coolprop);
//PressD = RefrigerantTPDP.deltap_JR(fluid, composition, d, g, p, x, l);
//PressD = RefrigerantTPDP.deltap_MS(fluid, composition, d, g, p, x, l);
htc_dp_single_sat = RefrigerantHTCandDP.HTCandDP_1p_sat(fluid, d, g, p, 1, l, coolprop); //x=1
href = (1 - lambdaV) * h_ref_2phase + lambdaV * htc_dp_single_sat.Href;
PressD = (1 - lambdaV) * deltap_2phase + lambdaV * htc_dp_single_sat.DPref;
}
}
else
{
if (x < 0.05 && x >= 0)
{
h_ref_2phase = RefrigerantTPHTC.Shah_Cond_href(fluid, d, g, p, x, q, l, coolprop);
//href = RefrigerantTPHTC.Dobson_Cond_href(fluid, composition, d, g, p, x, Ts, l);//需要考虑Ts的参数传递
deltap_2phase = RefrigerantTPDP.deltap_smooth(fluid, d, g, p, x, l, coolprop);
//PressD = RefrigerantTPDP.deltap_JR(fluid, composition, d, g, p, x, l);
//PressD = RefrigerantTPDP.deltap_MS(fluid, composition, d, g, p, x, l);
htc_dp_single_sat = RefrigerantHTCandDP.HTCandDP_1p_sat(fluid, d, g, p, 0, l, coolprop); //x=0
href = (1 - lambdaL) * htc_dp_single_sat.Href + lambdaL * h_ref_2phase;
PressD = (1 - lambdaL) * htc_dp_single_sat.DPref + lambdaL * deltap_2phase;
}
else if (x <= 0.9)
{
href = RefrigerantTPHTC.Shah_Cond_href(fluid, d, g, p, x, q, l, coolprop);
//href = RefrigerantTPHTC.Dobson_Cond_href(fluid, composition, d, g, p, x, Ts, l);//需要考虑Ts的参数传递
PressD = RefrigerantTPDP.deltap_smooth(fluid, d, g, p, x, l, coolprop);
//PressD = RefrigerantTPDP.deltap_JR(fluid, composition, d, g, p, x, l);
//PressD = RefrigerantTPDP.deltap_MS(fluid, composition, d, g, p, x, l);
}
else //vapor to 2-phase
{
h_ref_2phase = RefrigerantTPHTC.Shah_Cond_href(fluid, d, g, p, x, q, l, coolprop);
//href = RefrigerantTPHTC.Dobson_Cond_href(fluid, composition, d, g, p, x, Ts, l);//需要考虑Ts的参数传递
deltap_2phase = RefrigerantTPDP.deltap_smooth(fluid, d, g, p, x, l, coolprop);
//PressD = RefrigerantTPDP.deltap_JR(fluid, composition, d, g, p, x, l);
//PressD = RefrigerantTPDP.deltap_MS(fluid, composition, d, g, p, x, l);
htc_dp_single_sat = RefrigerantHTCandDP.HTCandDP_1p_sat(fluid, d, g, p, 1, l, coolprop); //x=1
href = (1 - lambdaV) * h_ref_2phase + lambdaV * htc_dp_single_sat.Href;
PressD = (1 - lambdaV) * deltap_2phase + lambdaV * htc_dp_single_sat.DPref;
}
//********divided to 3 region based on quality (0 - 0.05 - 0.95 - 1) to calculated HTC & DP END********
}
href = href * zh;
PressD = PressD * zdp;
return(new RefHTCandDPResult {
Href = href, DPref = PressD
});
}