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Initial commit for v5, but this time with the right line endings

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Signed-off-by: Ian bell <ian.h.bell@gmail.com>
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Ian bell
2014-05-14 12:46:24 +02:00
commit b3847c7522
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wrappers/Java/Example.java Normal file
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// Example for Java
// Ian Bell, 2013
public class Example {
static {
System.loadLibrary("CoolProp");
}
public static void main(String argv[]){
double T, h, p, D;
int SI,KSI;
System.out.println("CoolProp version: " + CoolProp.get_global_param_string("version"));
System.out.println("CoolProp gitrevision: " + CoolProp.get_global_param_string("gitrevision"));
System.out.println("CoolProp fluids: " + CoolProp.get_global_param_string("FluidsList"));
System.out.println(" ");
System.out.println("************ USING EOS *************");
System.out.println(" ");
System.out.println("FLUID STATE INDEPENDENT INPUTS");
//System.out.println("Critical Density Propane: " + CoolProp.Props1SI("Propane", "rhocrit") + "kg/m^3");
System.out.println("TWO PHASE INPUTS (Pressure)");
System.out.println("Density of saturated liquid Propane at 101325 kPa: " + CoolProp.PropsSI("D", "P", 101325, "Q", 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 101325 kPa: " + CoolProp.PropsSI("D", "P", 101325, "Q", 1, "R290") + " kg/m^3");
System.out.println("TWO PHASE INPUTS (Temperature)");
System.out.println("Density of saturated liquid Propane at 300 K: " + CoolProp.PropsSI("D", "T", 300, "Q", 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 300 K: " + CoolProp.PropsSI("D", "T", 300, "Q", 1, "R290") + " kg/m^3");
System.out.println("SINGLE PHASE CYCLE (propane)");
p = CoolProp.PropsSI("P", "T", 300, "D", 1, "Propane");
h = CoolProp.PropsSI("H", "T", 300, "D", 1, "Propane");
System.out.println("T,D -> P,H " + 300 + "," + 1 + " --> " + p + "," + h);
T = CoolProp.PropsSI("T", "P", p, "H", h, "Propane");
D = CoolProp.PropsSI("D", "P", p, "H", h, "Propane");
System.out.println("P,H -> T,D " + p + "," + h + " --> " + T + "," + D);
//~ System.out.println(" ");
//~ System.out.println("************ USING TTSE ***************");
//~ System.out.println(" ");
//~ CoolProp.enable_TTSE_LUT("Propane");
//~ System.out.println("TWO PHASE INPUTS (Pressure)");
//~ System.out.println("Density of saturated liquid Propane at 101325 kPa: " + CoolProp.PropsSI("D", "P", 101325, "Q", 0, "Propane") + " kg/m^3");
//~ System.out.println("Density of saturated vapor R290 at 101325 kPa: " + CoolProp.PropsSI("D", "P", 101325, "Q", 1, "R290") + " kg/m^3");
//~ System.out.println("TWO PHASE INPUTS (Temperature)");
//~ System.out.println("Density of saturated liquid Propane at 300 K: " + CoolProp.PropsSI("D", "T", 300, "Q", 0, "Propane") + " kg/m^3");
//~ System.out.println("Density of saturated vapor R290 at 300 K: " + CoolProp.PropsSI("D", "T", 300, "Q", 1, "R290") + " kg/m^3");
//~ System.out.println("SINGLE PHASE CYCLE (propane)");
//~ p = CoolProp.PropsSI("P", "T", 300, "D", 1, "Propane");
//~ h = CoolProp.PropsSI("H", "T", 300, "D", 1, "Propane");
//~ System.out.println("T,D -> P,H " + 300 + ","+ 1+ " --> " + p + "," + h);
//~ T = CoolProp.PropsSI("T", "P", p, "H", h, "Propane");
//~ D = CoolProp.PropsSI("D", "P", p, "H", h, "Propane");
//~ System.out.println("P,H -> T,D " + p + "," + h + " --> " + T + "," + D);
//~ CoolProp.disable_TTSE_LUT("Propane");
try
{
System.out.println(" ");
System.out.println("************ USING REFPROP ***************");
System.out.println(" ");
System.out.println("TWO PHASE INPUTS (Pressure)");
System.out.println("Density of saturated liquid Propane at 101325 kPa: " + CoolProp.PropsSI("D", "P", 101325, "Q", 0, "REFPROP::Propane") + " kg/m^3");
System.out.println("TWO PHASE INPUTS (Temperature)");
System.out.println("Density of saturated liquid Propane at 300 K: " + CoolProp.PropsSI("D", "T", 300, "Q", 0, "REFPROP::Propane") + " kg/m^3");
System.out.println("SINGLE PHASE CYCLE (propane)");
p = CoolProp.PropsSI("P","T",300,"D",1,"REFPROP::Propane");
h = CoolProp.PropsSI("H","T",300,"D",1,"REFPROP::Propane");
System.out.println("T,D -> P,H " + 300 + "," + 1 + " --> " + p + "," + h);
T = CoolProp.PropsSI("T","P",p,"H",h,"REFPROP::Propane");
D = CoolProp.PropsSI("D","P",p,"H",h,"REFPROP::Propane");
System.out.println("P,H -> T,D " + p + "," + h + " --> " + T + "," + D);
}
catch(Exception e)
{
System.out.println(" ");
System.out.println("************ CANT USE REFPROP ************");
System.out.println(" ");
}
System.out.println(" ");
System.out.println("************ BRINES AND SECONDARY WORKING FLUIDS *************");
System.out.println(" ");
System.out.println("Density of 50% (mass) ethylene glycol/water at 300 K, 101325 kPa: " + CoolProp.PropsSI("D", "T", 300, "P", 101325, "EG-50%") + "kg/m^3");
System.out.println("Viscosity of Therminol D12 at 350 K, 101325 kPa: " + CoolProp.PropsSI("V", "T", 350, "P", 101325, "TD12") + "Pa-s");
//~ System.out.println(" ");
//~ System.out.println("************ HUMID AIR PROPERTIES *************");
//~ System.out.println(" ");
//~ System.out.println("Humidity ratio of 50% rel. hum. air at 300 K, 101.325 kPa: " + CoolProp.HAProps("W", "T", 300, "P", 101.325, "R", 0.5) + " kg_w/kg_da");
//~ System.out.println("Relative humidity from last calculation: " + CoolProp.HAProps("R", "T", 300, "P", 101.325, "W", CoolProp.HAProps("W", "T", 300, "P", 101.325, "R", 0.5)) + "(fractional)");
}
}