using System;

namespace CapMachine.Wpf.PPCalculation
{
    /// <summary>
    /// 干度计算（基于焓法）的独立封装：
    /// - 先分别计算气路/液路阀前的单相质量比焓（TPRHO + THERM）
    /// - 再计算吸气压力对应的饱和液/饱和气质量比焓（SATP + THERM）
    /// - 最终按既定流程计算混合焓与干度，并限幅到 [0,1]
    /// 
    /// 注意：该类仅做封装以便维护，不应改变既有干度计算过程与逻辑。
    /// 调用方需确保 REFPROP 已完成 SETPATH/SETUP 初始化（与现有 PPCService 保持一致）。
    /// </summary>
    public sealed class EnthalpyDrynessCalculator
    {
        private readonly object _refpropLock;

        /// <summary>
        /// 构造函数。
        /// </summary>
        /// <param name="refpropLock">REFPROP 全局互斥锁对象（必须与系统其它 REFPROP 调用共用，以避免并发竞态）。</param>
        public EnthalpyDrynessCalculator(object refpropLock)
        {
            _refpropLock = refpropLock ?? throw new ArgumentNullException(nameof(refpropLock));
        }

        /// <summary>
        /// 干度计算输入模型（以 Tag 读数为准）。
        /// </summary>
        public readonly struct Input
        {
            public Input(
                double gasPreValvePressBarA,
                double gasPreValveTempC,
                double txvFrPressBarA,
                double txvFrTempC,
                double inhPressBarA,
                double vrvFlowKgPerH,
                double liqRefFlowKgPerH,
                double lubeFlowKgPerH)
            {
                GasPreValvePressBarA = gasPreValvePressBarA;
                GasPreValveTempC = gasPreValveTempC;
                TxvFrPressBarA = txvFrPressBarA;
                TxvFrTempC = txvFrTempC;
                InhPressBarA = inhPressBarA;
                VRVFlowKgPerH = vrvFlowKgPerH;
                LiqRefFlowKgPerH = liqRefFlowKgPerH;
                LubeFlowKgPerH = lubeFlowKgPerH;
            }

            public double GasPreValvePressBarA { get; }
            public double GasPreValveTempC { get; }
            public double TxvFrPressBarA { get; }
            public double TxvFrTempC { get; }
            public double InhPressBarA { get; }

            public double VRVFlowKgPerH { get; }
            public double LiqRefFlowKgPerH { get; }
            public double LubeFlowKgPerH { get; }
        }

        /// <summary>
        /// 干度计算输出模型。
        /// </summary>
        public readonly struct Result
        {
            public Result(
                double gasFlowKgPerH,
                double gasEnthalpy_kJkg,
                double liquidEnthalpy_kJkg,
                double satLiquidEnthalpy_kJkg,
                double satVaporEnthalpy_kJkg,
                bool isDryness1Success,
                double dryness1_01,
                double hMix1_kJkg,
                string error1,
                bool isDryness2Success,
                double dryness2_01,
                double hMix2_kJkg,
                string error2)
            {
                GasFlowKgPerH = gasFlowKgPerH;
                GasEnthalpy_kJkg = gasEnthalpy_kJkg;
                LiquidEnthalpy_kJkg = liquidEnthalpy_kJkg;
                SatLiquidEnthalpy_kJkg = satLiquidEnthalpy_kJkg;
                SatVaporEnthalpy_kJkg = satVaporEnthalpy_kJkg;

                IsDryness1Success = isDryness1Success;
                Dryness1_01 = dryness1_01;
                HMix1_kJkg = hMix1_kJkg;
                Error1 = error1 ?? string.Empty;

                IsDryness2Success = isDryness2Success;
                Dryness2_01 = dryness2_01;
                HMix2_kJkg = hMix2_kJkg;
                Error2 = error2 ?? string.Empty;
            }

            public double GasFlowKgPerH { get; }

            public double GasEnthalpy_kJkg { get; }
            public double LiquidEnthalpy_kJkg { get; }
            public double SatLiquidEnthalpy_kJkg { get; }
            public double SatVaporEnthalpy_kJkg { get; }

            public bool IsDryness1Success { get; }
            public double Dryness1_01 { get; }
            public double HMix1_kJkg { get; }
            public string Error1 { get; }

            public bool IsDryness2Success { get; }
            public double Dryness2_01 { get; }
            public double HMix2_kJkg { get; }
            public string Error2 { get; }
        }

        /// <summary>
        /// 按既有流程计算干度（两套：干度1/干度2）。
        /// </summary>
        /// <param name="input">输入数据。</param>
        /// <returns>计算结果。</returns>
        public Result Calculate(Input input)
        {
            // 气体流量 kg/h = 冷媒流量 kg/h - 液冷媒流量 kg/h
            double gasFlowKgPerH = input.VRVFlowKgPerH - input.LiqRefFlowKgPerH;

            // 定义气相质量焓 kJ/kg（注意：保持既有逻辑，默认 0，仅在成功计算时赋值）
            double gas_hVap_kJkg = 0.0;

            // 步骤1: 计算气路阀前气相焓 h_vap (单相气相)
            if (TryTPRHO_VaporDensity_ByTP_MPa_C(input.GasPreValvePressBarA * 0.1, input.GasPreValveTempC, out var dVap_molL, out _))
            {
                if (TryTHERM_VaporEnthalpy_ByTD(input.GasPreValveTempC, dVap_molL, out var hVap_kJkg, out _))
                {
                    gas_hVap_kJkg = hVap_kJkg;
                }
            }

            // 定义液相质量焓 kJ/kg（保持既有逻辑，默认 0，仅在成功计算时赋值）
            double liquid_hLiq_kJkg = 0.0;

            // 步骤2: 计算液路阀前液相焓 h_liq (单相液相)
            if (TryTPRHO_LiquidDensity_ByTP_MPa_C(input.TxvFrPressBarA * 0.1, input.TxvFrTempC, out var dLiq_molL, out _))
            {
                if (TryTHERM_LiquidEnthalpy_ByTD(input.TxvFrTempC, dLiq_molL, out var hLiq_kJkg, out _))
                {
                    liquid_hLiq_kJkg = hLiq_kJkg;
                }
            }

            // 定义饱和液/饱和气质量焓 kJ/kg（保持既有逻辑，默认 0，仅在同时成功时赋值）
            double hSatL_kJkg = 0.0;
            double hSatV_kJkg = 0.0;

            if (TryGetSaturationLiquidEnthalpy_ByP_MPa(input.InhPressBarA * 0.1, out var satL, out _) &&
                TryGetSaturationVaporEnthalpy_ByP_MPa(input.InhPressBarA * 0.1, out var satV, out _))
            {
                hSatL_kJkg = satL;
                hSatV_kJkg = satV;
            }

            // 干度1：mg=气体流量；ml=液体流量
            bool ok1 = TryComputeDrynessByEnthalpy(
                gas_hVap_kJkg,
                liquid_hLiq_kJkg,
                gasFlowKgPerH,
                input.LiqRefFlowKgPerH,
                hSatL_kJkg,
                hSatV_kJkg,
                out var dryness1,
                out var hMix1,
                out var err1);

            // 干度2：mg=气体流量+润滑油流量；ml=液体流量（保持既有策略）
            bool ok2 = TryComputeDrynessByEnthalpy2(
                gas_hVap_kJkg,
                liquid_hLiq_kJkg,
                gasFlowKgPerH,
                input.LubeFlowKgPerH,
                input.LiqRefFlowKgPerH,
                hSatL_kJkg,
                hSatV_kJkg,
                out var dryness2,
                out var hMix2,
                out var err2);

            return new Result(
                gasFlowKgPerH,
                gas_hVap_kJkg,
                liquid_hLiq_kJkg,
                hSatL_kJkg,
                hSatV_kJkg,
                ok1,
                dryness1,
                hMix1,
                err1,
                ok2,
                dryness2,
                hMix2,
                err2);
        }

        /// <summary>
        /// 获取指定组分的摩尔质量（kg/mol）。
        /// </summary>
        /// <param name="componentId">组分ID（icomp）。</param>
        /// <param name="molarMassKgPerMol">摩尔质量（kg/mol）。</param>
        /// <param name="error">错误信息。</param>
        /// <returns>是否成功。</returns>
        private bool TryGetMolarMassKgPerMol(long componentId, out double molarMassKgPerMol, out string error)
        {
            molarMassKgPerMol = double.NaN;
            error = string.Empty;

            try
            {
                double wmm = 0, Trp = 0, Tnbpt = 0, Tc = 0, Pc = 0, Dc = 0, Zc = 0, acf = 0, dip = 0, Rgas = 0;
                lock (_refpropLock)
                {
                    IRefProp64.INFOdll(ref componentId, ref wmm, ref Trp, ref Tnbpt, ref Tc, ref Pc, ref Dc, ref Zc, ref acf, ref dip, ref Rgas);
                }

                molarMassKgPerMol = wmm * 0.001;
                if (double.IsNaN(molarMassKgPerMol) || double.IsInfinity(molarMassKgPerMol) || molarMassKgPerMol <= 0)
                {
                    error = "无效的摩尔质量";
                    return false;
                }

                return true;
            }
            catch (Exception ex)
            {
                error = $"获取组分{componentId}的摩尔质量时出错: {ex.Message}";
                return false;
            }
        }

        /// <summary>
        /// TPRHOdll 封装：按 T(℃)、P(MPa) 计算“气相”摩尔密度 D [mol/L]（kph=2）。
        /// </summary>
        private bool TryTPRHO_VaporDensity_ByTP_MPa_C(double pressureMPa, double temperatureC, out double densityMolPerL, out string error)
        {
            densityMolPerL = double.NaN;
            error = string.Empty;

            double tK = temperatureC + 273.15;
            double pKPa = pressureMPa * 1000.0;

            double[] x = new double[20];
            x[0] = 1.0;

            long kph = 2;
            long kguess = 0;
            double D = 0.0;
            long ierr = 0;
            long herrLen = 255;
            string herr = new string(' ', 255);

            lock (_refpropLock)
            {
                IRefProp64.TPRHOdll(ref tK, ref pKPa, x, ref kph, ref kguess, ref D, ref ierr, ref herr, ref herrLen);
            }

            if (ierr != 0)
            {
                error = $"TPRHO 错误: {herr.Trim()} (ierr={ierr})";
                return false;
            }

            densityMolPerL = D;
            return true;
        }

        /// <summary>
        /// THERMdll 封装：按 T(℃) 与 D[mol/L] 计算气相质量焓 h_vap [kJ/kg]。
        /// </summary>
        private bool TryTHERM_VaporEnthalpy_ByTD(double temperatureC, double densityMolPerL, out double h_vap_kJ_per_kg, out string error)
        {
            h_vap_kJ_per_kg = double.NaN;
            error = string.Empty;

            double tK = temperatureC + 273.15;
            double D = densityMolPerL;

            double[] x = new double[20];
            x[0] = 1.0;

            double pOut = 0, e = 0, hJmol = 0, sJmolK = 0, cv = 0, cp = 0, w = 0, hjt = 0;

            if (!TryGetMolarMassKgPerMol(1, out var molarMassKgPerMol, out error))
            {
                return false;
            }

            lock (_refpropLock)
            {
                IRefProp64.THERMdll(ref tK, ref D, x, ref pOut, ref e, ref hJmol, ref sJmolK, ref cv, ref cp, ref w, ref hjt);
            }

            h_vap_kJ_per_kg = (hJmol / molarMassKgPerMol) * 0.001;
            return true;
        }

        /// <summary>
        /// TPRHOdll 封装：按 T(℃)、P(MPa) 计算“液相”摩尔密度 D [mol/L]（kph=1）。
        /// </summary>
        private bool TryTPRHO_LiquidDensity_ByTP_MPa_C(double pressureMPa, double temperatureC, out double densityMolPerL, out string error)
        {
            densityMolPerL = double.NaN;
            error = string.Empty;

            double tK = temperatureC + 273.15;
            double pKPa = pressureMPa * 1000.0;

            double[] x = new double[20];
            x[0] = 1.0;

            long kph = 1;
            long kguess = 0;
            double D = 0.0;
            long ierr = 0;
            long herrLen = 255;
            string herr = new string(' ', 255);

            lock (_refpropLock)
            {
                IRefProp64.TPRHOdll(ref tK, ref pKPa, x, ref kph, ref kguess, ref D, ref ierr, ref herr, ref herrLen);
            }

            if (ierr != 0)
            {
                error = $"TPRHO(液相) 错误: {herr.Trim()} (ierr={ierr})";
                return false;
            }

            densityMolPerL = D;
            return true;
        }

        /// <summary>
        /// THERMdll 封装：按 T(℃) 与 D[mol/L] 计算液相质量焓 h_liq [kJ/kg]。
        /// </summary>
        private bool TryTHERM_LiquidEnthalpy_ByTD(double temperatureC, double densityMolPerL, out double h_liq_kJ_per_kg, out string error)
        {
            h_liq_kJ_per_kg = double.NaN;
            error = string.Empty;

            double tK = temperatureC + 273.15;
            double D = densityMolPerL;

            double[] x = new double[20];
            x[0] = 1.0;

            double pOut = 0, e = 0, hJmol = 0, sJmolK = 0, cv = 0, cp = 0, w = 0, hjt = 0;

            if (!TryGetMolarMassKgPerMol(1, out var molarMassKgPerMol, out error))
            {
                return false;
            }

            lock (_refpropLock)
            {
                IRefProp64.THERMdll(ref tK, ref D, x, ref pOut, ref e, ref hJmol, ref sJmolK, ref cv, ref cp, ref w, ref hjt);
            }

            h_liq_kJ_per_kg = (hJmol / molarMassKgPerMol) * 0.001;
            return true;
        }

        /// <summary>
        /// SATPdll：由压力 P(MPa) 求饱和温度 Tsat[K]、饱和液/气摩尔密度 Dl/Dv [mol/L]。
        /// </summary>
        private bool TrySATP_SaturationByP_MPa(double pressureMPa, out double tSatK, out double Dl_molL, out double Dv_molL, out string error)
        {
            tSatK = double.NaN;
            Dl_molL = double.NaN;
            Dv_molL = double.NaN;
            error = string.Empty;

            double pKPa = pressureMPa * 1000.0;
            double[] x = new double[20];
            x[0] = 1.0;

            long kph = 1;
            double Dl = 0, Dv = 0;
            double[] xliq = new double[20];
            double[] xvap = new double[20];
            long ierr = 0, herrLen = 255;
            string herr = new string(' ', 255);

            lock (_refpropLock)
            {
                IRefProp64.SATPdll(ref pKPa, x, ref kph, ref tSatK, ref Dl, ref Dv, xliq, xvap, ref ierr, ref herr, ref herrLen);
            }

            if (ierr != 0)
            {
                error = $"SATP 错误: {herr.Trim()} (ierr={ierr})";
                return false;
            }

            Dl_molL = Dl;
            Dv_molL = Dv;
            return true;
        }

        /// <summary>
        /// THERMdll：由 T[K] 与 D[mol/L] 计算质量比焓 h[kJ/kg]。
        /// </summary>
        private bool TryTHERM_Enthalpy_kJkg_ByT_K_D(double temperatureK, double densityMolPerL, out double h_kJ_per_kg, out string error)
        {
            h_kJ_per_kg = double.NaN;
            error = string.Empty;

            double tK = temperatureK;
            double D = densityMolPerL;

            double[] x = new double[20];
            x[0] = 1.0;

            double pOut = 0, e = 0, hJmol = 0, sJmolK = 0, cv = 0, cp = 0, w = 0, hjt = 0;

            if (!TryGetMolarMassKgPerMol(1, out var molarMassKgPerMol, out error))
            {
                return false;
            }

            lock (_refpropLock)
            {
                IRefProp64.THERMdll(ref tK, ref D, x, ref pOut, ref e, ref hJmol, ref sJmolK, ref cv, ref cp, ref w, ref hjt);
            }

            h_kJ_per_kg = (hJmol / molarMassKgPerMol) * 0.001;
            return true;
        }

        /// <summary>
        /// 便捷：由压力 P(MPa) 直接得到“饱和液”质量比焓 h_liq[kJ/kg]。
        /// </summary>
        private bool TryGetSaturationLiquidEnthalpy_ByP_MPa(double pressureMPa, out double h_liq_kJkg, out string error)
        {
            h_liq_kJkg = double.NaN;
            error = string.Empty;

            if (!TrySATP_SaturationByP_MPa(pressureMPa, out double tSatK, out double Dl, out _, out error))
            {
                return false;
            }

            return TryTHERM_Enthalpy_kJkg_ByT_K_D(tSatK, Dl, out h_liq_kJkg, out error);
        }

        /// <summary>
        /// 便捷：由压力 P(MPa) 直接得到“饱和气”质量比焓 h_vap[kJ/kg]。
        /// </summary>
        private bool TryGetSaturationVaporEnthalpy_ByP_MPa(double pressureMPa, out double h_vap_kJkg, out string error)
        {
            h_vap_kJkg = double.NaN;
            error = string.Empty;

            if (!TrySATP_SaturationByP_MPa(pressureMPa, out double tSatK, out _, out double Dv, out error))
            {
                return false;
            }

            return TryTHERM_Enthalpy_kJkg_ByT_K_D(tSatK, Dv, out h_vap_kJkg, out error);
        }

        /// <summary>
        /// 按图片的最终流程计算干度：
        /// 1) 质量流量加权混合焓 h_mix = (h_vap*mg + h_liq*ml) / (mg + ml)
        /// 2) 干度 x = (h_mix - h_l) / (h_v - h_l)，并限幅到 [0,1]
        /// 
        /// 入参单位：
        /// - hVap_kJkg, hLiq_kJkg, hSatL_kJkg, hSatV_kJkg 均为 kJ/kg
        /// - mGas_kg_h, mLiq_kg_h 均为 kg/h
        /// </summary>
        private bool TryComputeDrynessByEnthalpy(
            double hVap_kJkg,
            double hLiq_kJkg,
            double mGas_kg_h,
            double mLiq_kg_h,
            double hSatL_kJkg,
            double hSatV_kJkg,
            out double dryness,
            out double hMix_kJkg,
            out string error)
        {
            dryness = double.NaN;
            hMix_kJkg = double.NaN;
            error = string.Empty;

            if (double.IsNaN(hVap_kJkg) || double.IsNaN(hLiq_kJkg) || double.IsNaN(hSatL_kJkg) || double.IsNaN(hSatV_kJkg))
            {
                error = "输入焓值存在 NaN";
                return false;
            }
            if (double.IsNaN(mGas_kg_h) || double.IsNaN(mLiq_kg_h))
            {
                error = "输入质量流量存在 NaN";
                return false;
            }

            double mg = Math.Max(0.0, mGas_kg_h);
            double ml = Math.Max(0.0, mLiq_kg_h);
            double mSum = mg + ml;
            if (mSum <= 0)
            {
                error = "气液质量流量之和为 0，无法进行加权混合焓计算";
                return false;
            }

            hMix_kJkg = (hVap_kJkg * mg + hLiq_kJkg * ml) / mSum;

            double denom = (hSatV_kJkg - hSatL_kJkg);
            const double eps = 1e-9;
            if (Math.Abs(denom) < eps)
            {
                error = "饱和气/液焓差过小，无法计算干度（可能接近临界点或输入异常）";
                return false;
            }

            double x = (hMix_kJkg - hSatL_kJkg) / denom;

            if (double.IsNaN(x) || double.IsInfinity(x))
            {
                error = "干度计算结果异常（NaN/Inf）";
                return false;
            }

            dryness = Math.Min(1.0, Math.Max(0.0, x));
            return true;
        }

        /// <summary>
        /// 按图片的最终流程计算干度2：
        /// 计算逻辑同干度1，但气体流量 mg = 气体流量 + 润滑油流量。
        /// </summary>
        private bool TryComputeDrynessByEnthalpy2(
            double hVap_kJkg,
            double hLiq_kJkg,
            double mGas_kg_h,
            double lubeFlow_kg_h,
            double mLiq_kg_h,
            double hSatL_kJkg,
            double hSatV_kJkg,
            out double dryness,
            out double hMix_kJkg,
            out string error)
        {
            dryness = double.NaN;
            hMix_kJkg = double.NaN;
            error = string.Empty;

            if (double.IsNaN(hVap_kJkg) || double.IsNaN(hLiq_kJkg) || double.IsNaN(hSatL_kJkg) || double.IsNaN(hSatV_kJkg))
            {
                error = "输入焓值存在 NaN";
                return false;
            }
            if (double.IsNaN(mGas_kg_h) || double.IsNaN(mLiq_kg_h))
            {
                error = "输入质量流量存在 NaN";
                return false;
            }

            double mg = Math.Max(0.0, mGas_kg_h) + Math.Max(0.0, lubeFlow_kg_h);
            double ml = Math.Max(0.0, mLiq_kg_h);
            double mSum = mg + ml;
            if (mSum <= 0)
            {
                error = "气液质量流量之和为 0，无法进行加权混合焓计算";
                return false;
            }

            hMix_kJkg = (hVap_kJkg * mg + hLiq_kJkg * ml) / mSum;

            double denom = (hSatV_kJkg - hSatL_kJkg);
            const double eps = 1e-9;
            if (Math.Abs(denom) < eps)
            {
                error = "饱和气/液焓差过小，无法计算干度（可能接近临界点或输入异常）";
                return false;
            }

            double x = (hMix_kJkg - hSatL_kJkg) / denom;

            if (double.IsNaN(x) || double.IsInfinity(x))
            {
                error = "干度计算结果异常（NaN/Inf）";
                return false;
            }

            dryness = Math.Min(1.0, Math.Max(0.0, x));
            return true;
        }
    }
}