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Tyrone CT
2025-10-14 14:40:52 +08:00
parent 7a2eca6f2f
commit 5849d0cb5d
1 changed files with 27 additions and 24 deletions
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43
CapMachine.Wpf/Services/PPCService.cs
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@@ -357,15 +357,15 @@ namespace CapMachine.Wpf.Services
{ {
string dryErr; string dryErr;
double ps = InhPressTag.PVModel.EngValue;//吸气压力 double ps = InhPressTag.PVModel.EngValue;//吸气压力
ps = 2.374421;//Mpa ->BarA //ps = 2.374421;//Mpa ->BarA
double pg = GasPreValvePressTag.PVModel.EngValue;//气路阀前压力 double pg = GasPreValvePressTag.PVModel.EngValue;//气路阀前压力
pg = 19.77032;//Mpa ->BarA //pg = 19.77032;//Mpa ->BarA
double tg = GasPreValveTempTag.PVModel.EngValue;//气路阀前温度 double tg = GasPreValveTempTag.PVModel.EngValue;//气路阀前温度
tg = 61.76869; //tg = 61.76869;
double plv = TxvFrPressTag.PVModel.EngValue;//膨胀阀前压力=液路阀前压力 double plv = TxvFrPressTag.PVModel.EngValue;//膨胀阀前压力=液路阀前压力
plv = 19.26757;//Mpa ->BarA //plv = 19.26757;//Mpa ->BarA
double tlv = TxvFrTempTag.PVModel.EngValue;//膨胀阀前温度 = SUBCOOL出口温度 =液路阀前温度 double tlv = TxvFrTempTag.PVModel.EngValue;//膨胀阀前温度 = SUBCOOL出口温度 =液路阀前温度
tlv = 64.96428; //tlv = 64.96428;
//液体流量=液冷媒流量 kg/h //液体流量=液冷媒流量 kg/h
//气体流量=冷媒流量-液体流量 kg/h //气体流量=冷媒流量-液体流量 kg/h
@@ -373,19 +373,22 @@ namespace CapMachine.Wpf.Services
double GasMassFlowKgPerH, LiquidMassFlowKgPerH; double GasMassFlowKgPerH, LiquidMassFlowKgPerH;
LiquidMassFlowKgPerH = LiqRefFlowTag.PVModel.EngValue; // [kg/h] LiquidMassFlowKgPerH = LiqRefFlowTag.PVModel.EngValue; // [kg/h]
// VRV 为体积流量 [L/min]，需结合管段相态与 T/P 计算密度后换算为质量流量 [kg/h] GasMassFlowKgPerH = (double)(VRVTag?.PVModel?.EngValue - LiquidMassFlowKgPerH);
double vrvLmin = VRVTag?.PVModel?.EngValue ?? 0.0;
double totalMassKgPerH; ////单位转换和数据计算
string flowErr; //// VRV 为体积流量 [L/min]，需结合管段相态与 T/P 计算密度后换算为质量流量 [kg/h]
if (TryConvertVolumetricFlowLMinToMassKgPerH(vrvLmin, plv, tlv, 1, out totalMassKgPerH, out flowErr)) // 1=液相（若 VRV 在液管） //double vrvLmin = VRVTag?.PVModel?.EngValue ?? 0.0;
{ //double totalMassKgPerH;
GasMassFlowKgPerH = Math.Max(0.0, totalMassKgPerH - LiquidMassFlowKgPerH); //string flowErr;
} //if (TryConvertVolumetricFlowLMinToMassKgPerH(vrvLmin, plv, tlv, 1, out totalMassKgPerH, out flowErr)) // 1=液相（若 VRV 在液管）
else //{
{ // GasMassFlowKgPerH = Math.Max(0.0, totalMassKgPerH - LiquidMassFlowKgPerH);
Logger.Warn($"VRV 体积流量→质量流量换算失败：{flowErr}。已将气体质量流量置 0。输入: VRV={vrvLmin:F3} L/min, Pl={plv:F3} BarA, Tl={tlv:F3} ℃"); //}
GasMassFlowKgPerH = 0.0; //else
} //{
// Logger.Warn($"VRV 体积流量→质量流量换算失败：{flowErr}。已将气体质量流量置 0。输入: VRV={vrvLmin:F3} L/min, Pl={plv:F3} BarA, Tl={tlv:F3} ℃");
// GasMassFlowKgPerH = 0.0;
//}
//LiquidMassFlowKgPerH = 214.3051; //LiquidMassFlowKgPerH = 214.3051;
//GasMassFlowKgPerH = 264.7956- 214.3051; //GasMassFlowKgPerH = 264.7956- 214.3051;
@@ -424,8 +427,8 @@ namespace CapMachine.Wpf.Services
kph = 1; kph = 1;
p1 = (TxvFrPressTag.PVModel.EngValue) * 100.0;//textBox3 Evap.膨胀阀前压力（BarA→kPa） p1 = (TxvFrPressTag.PVModel.EngValue) * 100.0;//textBox3 Evap.膨胀阀前压力（BarA→kPa）
//p1 = Convert.ToDouble(textBox3.Text) * 100.0;//textBox3 Evap.膨胀阀前压力（BarA→kPa） //p1 = Convert.ToDouble(textBox3.Text) * 100.0;//textBox3 Evap.膨胀阀前压力（BarA→kPa）
// 重复的 SATP 与干度计算已在上方 lock(_refpropLock) 中统一完成，此处移除重复调用 // 重复的 SATP 与干度计算已在上方 lock(_refpropLock) 中统一完成，此处移除重复调用
} }
catch (Exception ex) catch (Exception ex)
{ {