CoolProp/Web/examples/CSharp/Example.cs

using System;
using System.Collections.Generic;
using System.Linq;
using System.Text;

namespace ConsoleApplication1
{
    class Program
    {
        static void Main(string[] args)
        {
            double T, h, p, D;
            Console.Write("CoolProp version: " + CoolProp.get_global_param_string("version") + "\n");
            Console.Write("CoolProp gitrevision: " + CoolProp.get_global_param_string("gitrevision") + "\n");
            Console.Write("CoolProp fluids: " + CoolProp.get_global_param_string("FluidsList") + "\n");

            Console.Write(" " + "\n");
            Console.Write("************ USING EOS *************" + "\n");
            Console.Write(" " + "\n");
            Console.Write("FLUID STATE INDEPENDENT INPUTS" + "\n");
            Console.Write("Critical Density Propane: " + CoolProp.Props1("Propane", "rhocrit") + "kg/m^3" + "\n");
            Console.Write("TWO PHASE INPUTS (Pressure)" + "\n");
            Console.Write("Density of saturated liquid Propane at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 0, "Propane") + " kg/m^3" + "\n");
            Console.Write("Density of saturated vapor R290 at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 1, "R290") + " kg/m^3" + "\n");
            Console.Write("TWO PHASE INPUTS (Temperature)" + "\n");
            Console.Write("Density of saturated liquid Propane at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 0, "Propane") + " kg/m^3" + "\n");
            Console.Write("Density of saturated vapor R290 at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 1, "R290") + " kg/m^3" + "\n");
            Console.Write("SINGLE PHASE CYCLE (propane)" + "\n");
            p = CoolProp.Props("P", 'T', 300, 'D', 1, "Propane");
            h = CoolProp.Props("H", 'T', 300, 'D', 1, "Propane");
            Console.Write("T,D -> P,H " + 300 + "," + 1 + " --> " + p + ',' + h + "\n");
            T = CoolProp.Props("T", 'P', p, 'H', h, "Propane");
            D = CoolProp.Props("D", 'P', p, 'H', h, "Propane");
            Console.Write("P,H -> T,D " + p + ',' + h + " --> " + T + ',' + D + "\n");

            Console.Write(" " + "\n");
            Console.Write("************ USING TTSE ***************" + "\n");
            Console.Write(" " + "\n");
            CoolProp.enable_TTSE_LUT("Propane");
            Console.Write("TWO PHASE INPUTS (Pressure)" + "\n");
            Console.Write("Density of saturated liquid Propane at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 0, "Propane") + " kg/m^3" + "\n");
            Console.Write("Density of saturated vapor R290 at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 1, "R290") + " kg/m^3" + "\n");
            Console.Write("TWO PHASE INPUTS (Temperature)" + "\n");
            Console.Write("Density of saturated liquid Propane at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 0, "Propane") + " kg/m^3" + "\n");
            Console.Write("Density of saturated vapor R290 at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 1, "R290") + " kg/m^3" + "\n");
            Console.Write("SINGLE PHASE CYCLE (propane)" + "\n");
            p = CoolProp.Props("P", 'T', 300, 'D', 1, "Propane");
            h = CoolProp.Props("H", 'T', 300, 'D', 1, "Propane");
            Console.Write("T,D -> P,H " + 300 + ","+ 1+ " --> " + p + ',' + h + "\n");
            T = CoolProp.Props("T", 'P', p, 'H', h, "Propane");
            D = CoolProp.Props("D", 'P', p, 'H', h, "Propane");
            Console.Write("P,H -> T,D " + p + ',' + h + " --> " + T + ',' + D + "\n");
            CoolProp.disable_TTSE_LUT("Propane");

            try
            {
                Console.Write(" " + "\n");
                Console.Write("************ USING REFPROP ***************" + "\n");
                Console.Write(" " + "\n");
                Console.Write("TWO PHASE INPUTS (Pressure)" + "\n");
                Console.Write("Density of saturated liquid Propane at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 0, "Propane") + " kg/m^3" + "\n");
                Console.Write("Density of saturated vapor R290 at 101.325 kPa: " + CoolProp.Props("D", 'P', 101.325, 'Q', 1, "R290") + " kg/m^3" + "\n");
                Console.Write("TWO PHASE INPUTS (Temperature)" + "\n");
                Console.Write("Density of saturated liquid Propane at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 0, "Propane") + " kg/m^3" + "\n");
                Console.Write("Density of saturated vapor R290 at 300 K: " + CoolProp.Props("D", 'T', 300, 'Q', 1, "R290") + " kg/m^3" + "\n");
                Console.Write("SINGLE PHASE CYCLE (propane)" + "\n");
                p = CoolProp.Props("P",'T',300,'D',1,"Propane"); 
                h = CoolProp.Props("H",'T',300,'D',1,"Propane");
                Console.Write("T,D -> P,H " + 300 + "," + 1 + " --> " + p + ',' + h + "\n");
                T = CoolProp.Props("T",'P',p,'H',h,"Propane"); 
                D = CoolProp.Props("D",'P',p,'H',h,"Propane");
                Console.Write("P,H -> T,D " + p + ',' + h + " --> " + T + ',' + D + "\n");
            }
            catch
            {
                Console.Write(" " + "\n");
                Console.Write("************ CANT USE REFPROP ************" + "\n");
                Console.Write(" " + "\n");
            }

            Console.Write(" " + "\n");
            Console.Write("************ CHANGE UNIT SYSTEM (default is kSI) *************" + "\n");
            Console.Write(" " + "\n");
            int SI = (int)unit_systems.UNIT_SYSTEM_SI;
            int kSI = (int)unit_systems.UNIT_SYSTEM_KSI;
            CoolProp.set_standard_unit_system(SI);
            Console.Write("Vapor pressure of water at 373.15 K in SI units (Pa): " + CoolProp.Props("P", 'T', 373.15, 'Q', 0, "Water") + "\n");
            CoolProp.set_standard_unit_system(kSI);
            Console.Write("Vapor pressure of water at 373.15 K in kSI units (kPa): " + CoolProp.Props("P", 'T', 373.15, 'Q', 0, "Water") + "\n");

            Console.Write(" " + "\n");
            Console.Write("************ BRINES AND SECONDARY WORKING FLUIDS *************" + "\n");
            Console.Write(" " + "\n");
            Console.Write("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" + "\n");
            Console.Write("Viscosity of Therminol D12 at 350 K, 101.325 kPa: " + CoolProp.Props("V", 'T', 350, 'P', 101.325, "TD12") + "Pa-s" + "\n");

            Console.Write(" " + "\n");
            Console.Write("************ HUMID AIR PROPERTIES *************" + "\n");
            Console.Write(" " + "\n");
            Console.Write("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" + "\n");
            Console.Write("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)" + "\n");

            //Console.Write("Enter to quit");
            //Console.ReadLine();
        }
    }
}