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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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Web/examples/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.Props1("Propane", "rhocrit") + "kg/m^3");
System.out.println("TWO PHASE INPUTS (Pressure)");
System.out.println("Density of saturated liquid Propane at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, '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.Props("D", 'T', 300, 'Q', 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 1, "R290") + " kg/m^3");
System.out.println("SINGLE PHASE CYCLE (propane)");
p = CoolProp.Props("P", 'T', 300, 'D', 1, "Propane");
h = CoolProp.Props("H", 'T', 300, 'D', 1, "Propane");
System.out.println("T,D -> P,H " + 300 + "," + 1 + " --> " + p + ',' + h);
T = CoolProp.Props("T", 'P', p, 'H', h, "Propane");
D = CoolProp.Props("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 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, '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.Props("D", 'T', 300, 'Q', 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 1, "R290") + " kg/m^3");
System.out.println("SINGLE PHASE CYCLE (propane)");
p = CoolProp.Props("P", 'T', 300, 'D', 1, "Propane");
h = CoolProp.Props("H", 'T', 300, 'D', 1, "Propane");
System.out.println("T,D -> P,H " + 300 + ","+ 1+ " --> " + p + ',' + h);
T = CoolProp.Props("T", 'P', p, 'H', h, "Propane");
D = CoolProp.Props("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 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, '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.Props("D", 'T', 300, 'Q', 0, "Propane") + " kg/m^3");
System.out.println("Density of saturated vapor R290 at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 1, "R290") + " kg/m^3");
System.out.println("SINGLE PHASE CYCLE (propane)");
p = CoolProp.Props("P",'T',300,'D',1,"Propane");
h = CoolProp.Props("H",'T',300,'D',1,"Propane");
System.out.println("T,D -> P,H " + 300 + "," + 1 + " --> " + p + ',' + h);
T = CoolProp.Props("T",'P',p,'H',h,"Propane");
D = CoolProp.Props("D",'P',p,'H',h,"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("************ CHANGE UNIT SYSTEM (default is kSI) *************");
System.out.println(" ");
CoolProp.set_standard_unit_system(unit_systems.UNIT_SYSTEM_SI.swigValue());
System.out.println("Vapor pressure of water at 373.15 K in SI units (Pa): " + CoolProp.Props("P", 'T', 373.15, 'Q', 0, "Water"));
CoolProp.set_standard_unit_system(unit_systems.UNIT_SYSTEM_KSI.swigValue());
System.out.println("Vapor pressure of water at 373.15 K in kSI units (kPa): " + CoolProp.Props("P", 'T', 373.15, 'Q', 0, "Water"));
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, 101.325 kPa: " + CoolProp.Props("D", 'T', 300, 'P', 101.325, "EG-50%") + "kg/m^3");
System.out.println("Viscosity of Therminol D12 at 350 K, 101.325 kPa: " + CoolProp.Props("V", 'T', 350, 'P', 101.325, "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)");
}
}