public void TestMethod1()
{
var geoInput = new GeometryInput();
var refInput = new RefStateInput();
var airInput = new AirStateInput();
CapiliaryInput capInput = new CapiliaryInput();
//ref input
refInput.FluidName = "R32";
AbstractState coolprop = AbstractState.factory("HEOS", refInput.FluidName);
refInput.Massflowrate = 0.01870031119662376; //kg/s
for (int i = 0; i < 20; i++)
{
//for condenser
refInput.tc = 45;
refInput.tri = 80;
//for evaporator
//refInput.te = 280 - 273.15;
//refInput.P_exv = CoolProp.PropsSI("P", "T", refInput.tc + 273.15, "Q", 0, refInput.FluidName) / 1000;
//refInput.T_exv = refInput.tc - 8;
//refInput.H_exv = 250;
//air input
airInput.Volumetricflowrate = 0.01 + i * 0.025789474; //m3/s
airInput.tai = 25;
airInput.RHi = 0.5;
airInput.ha = 80;
//geo input, mm
geoInput.Pt = 21;
geoInput.Pr = 22;
geoInput.Di = 6.9;
geoInput.Do = 7.4;
geoInput.L = 842;
geoInput.FPI = 21;
geoInput.Fthickness = 0.095;
geoInput.Nrow = 2;
geoInput.Ntube = 24;
geoInput.CirNum = 2;
//cap input
capInput.d_cap = new double[] { 0.006, 0.006 };
capInput.lenth_cap = new double[] { 0.5, 0.5 };
DateTime Time1 = DateTime.Now;
var rr = Main.main_condenser_py(refInput, airInput, geoInput, Model.HumidAirSourceData.SourceTableData);
DateTime Time2 = DateTime.Now;
double time = (Time2 - Time1).TotalSeconds;
using (StreamWriter wr = File.AppendText(@"D:\Work\Simulation\Test\smoothness.txt"))
{
wr.WriteLine("v, {0}, href, {1}, PressD, {2}, Q, {3}, Xo, {4}, Tro, {5}, Hro, {6}, Charge, {7}, Time, {8}", airInput.Volumetricflowrate, rr.href, rr.DP, rr.Q, rr.x_o, rr.Tro, rr.hro, rr.M, time);
}
}
//var r = Main.main_evaporator_py(refInput, airInput, geoInput);
}
public void TestMethod1(double[,] SourceTableData)
{
//var r = Main.main_evaporator();
//var r1 = Main.main_condenser();
RefStateInput refInput = new RefStateInput();
CapiliaryInput cap_inlet = new CapiliaryInput();
CapiliaryInput cap_outlet = new CapiliaryInput();
refInput.FluidName = "R32";
AbstractState coolprop = AbstractState.factory("HEOS", refInput.FluidName);
refInput.Massflowrate = 0.005;
refInput.tc = 45;
refInput.tri = 75;
AirStateInput airInput = new AirStateInput();
airInput.RHi = 0.5;
airInput.tai = 35;
airInput.Volumetricflowrate = 1000;
GeometryInput geoInput = new GeometryInput();
geoInput.Pt = 21;
geoInput.Pr = 22;
geoInput.Di = 6.9;
geoInput.Do = 7.4;
geoInput.L = 600;
geoInput.FPI = 1.3;
geoInput.Fthickness = 0.095;
geoInput.Nrow = 2;
geoInput.Ntube = 14;
geoInput.CirNum = 3;
// cap input
cap_inlet.d_cap = new double[6]; // { 0, 0 };//0.006
cap_inlet.lenth_cap = new double[6]; // { 0, 0 };//0.5
cap_outlet.d_cap = new double[6]; // { 0, 0 };//0.006
cap_outlet.lenth_cap = new double[6]; // { 0, 0 };//0.5
string flowtype = "逆流";
string fin_type = "平片";
string tube_type = "光管";
string hex_type = "冷凝器";
var r1 = Main.main_condenser_Slab(refInput, airInput, geoInput, flowtype, fin_type, tube_type, hex_type, cap_inlet, cap_outlet, SourceTableData);
//var r = Main.MinNout();
//var r = Main.NinMout();
}
public void TestMethod1()
{
var geoInput = new GeometryInput();
var refInput = new RefStateInput();
var airInput = new AirStateInput();
CapiliaryInput capInput = new CapiliaryInput();
//ref input
refInput.FluidName = "R32";
AbstractState coolprop = AbstractState.factory("HEOS", refInput.FluidName);
//*************if input SC or Sh, Massflowrate is the initial input***************
refInput.Massflowrate = 0.02161311486;//0.02 //kg/s
refInput.zh = 1.6;
refInput.zdp = 4;
airInput.za = 1;
airInput.zdpa = 1.0;
//for condenser
refInput.tc = 45;
refInput.tri = 80;
//refInput.tc = 40;
//refInput.tri = 70;
//for evaporator
refInput.te = 6.92842345;//12
//refInput.P_exv = CoolProp.PropsSI("P", "T", refInput.tc + 273.15, "Q", 0, refInput.FluidName) / 1000;
coolprop.update(input_pairs.QT_INPUTS, 0, refInput.tc + 273.15);
refInput.P_exv = coolprop.p() / 1000;
refInput.T_exv = refInput.tc - 8;
refInput.H_exv = 272;
//air input
airInput.Volumetricflowrate = 0.23; //m3/s
airInput.tai = 27; //24.85
airInput.RHi = 0.47;
//airInput.ha = 80;
//geo input
//mm
geoInput.Pt = 21;
geoInput.Pr = 13.37;
geoInput.Di = 6.89;
geoInput.Do = 7.35;
geoInput.L = 653;
geoInput.FPI = 21;
geoInput.Fthickness = 0.095;
geoInput.Nrow = 2;
geoInput.Ntube = 15;
geoInput.CirNum = 2;
//初始化湿空气数组
double[,] HumidSourceData = Model.HumidAirSourceData.InitializeSourceTableData();
DateTime Time1 = DateTime.Now;
//var rr = Main.main_condenser_py(refInput, airInput, geoInput, capInput, coolprop, Model.HumidAirSourceData.SourceTableData);
//var r = Main.main_evaporator_py(refInput, airInput, geoInput, capInput, coolprop, HumidAirSourceData.SourceTableData);
var rr = Main.main_condenser_py(refInput, airInput, geoInput, HumidSourceData);
var r = Main.main_evaporator_py(refInput, airInput, geoInput, HumidSourceData);
//for (int i=0;i<5;i++)
//r = Main.main_evaporator_py(refInput, airInput, geoInput, capInput);
//DateTime Time2 = DateTime.Now;
//double time01 = (Time2 - Time1).TotalSeconds;
//using (StreamWriter wr = File.AppendText(@"D:\QQQ.txt"))
//{
// for (int i = 0; i < 10; i++)
// {
// refInput.H_exv = 270 + i;
// var r = Main.main_evaporator_py(refInput, airInput, geoInput, HumidSourceData);
// wr.WriteLine("{0}", r.Q);
// }
//}
//using (StreamWriter wr = File.AppendText(@"D:\QQQ.txt"))
//{
// for (int i = 0; i < 15; i++)
// {
// for (int j = 0; j < 2;j++ )
// {
// wr.WriteLine("{0}", r.Q_detail[i,j]);
// }
// }
//}
//double Tsc_set = 5;
//double Tsh_set = 5;
//var rr = Main.main_condenser_inputSC_py(Tsc_set, refInput, airInput, geoInput, capInput, coolprop);
//var rrr = Main.main_evaporator_inputSH_py(Tsh_set, refInput, airInput, geoInput, capInput, coolprop);
DateTime Time2 = DateTime.Now;
double time01 = (Time2 - Time1).TotalSeconds;
}