Known bad point (unphysical energy loss)
This commit is contained in:
@@ -67,6 +67,8 @@ namespace FluidSim.Components
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_fxR_mass = m; _fxR_mom = p; _fxR_ener = e; _rightSet = true;
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_fxR_mass = m; _fxR_mom = p; _fxR_ener = e; _rightSet = true;
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}
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}
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public void Simulate()
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public void Simulate()
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{
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{
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int n = _n;
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int n = _n;
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@@ -106,16 +108,15 @@ namespace FluidSim.Components
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if (_E[i] < kinetic) _E[i] = kinetic;
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if (_E[i] < kinetic) _E[i] = kinetic;
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}
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}
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// Friction
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// Friction (energy‑conserving)
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if (FrictionFactor > 0)
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if (FrictionFactor > 0)
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{
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{
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double D = 2.0 * Math.Sqrt(_area / Math.PI);
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double D = 2.0 * Math.Sqrt(_area / Math.PI);
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for (int i = 0; i < n; i++)
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for (int i = 0; i < _n; i++)
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{
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{
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double u = _rhou[i] / Math.Max(_rho[i], 1e-12);
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double u = _rhou[i] / Math.Max(_rho[i], 1e-12);
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double f = FrictionFactor / (2.0 * D) * _rho[i] * u * Math.Abs(u);
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double f = FrictionFactor / (2.0 * D) * _rho[i] * u * Math.Abs(u);
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_rhou[i] -= _dt * f;
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//_rhou[i] -= _dt * f; FRICTIN DISABLED!!!
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if (_E[i] > _dt * f * u) _E[i] -= _dt * f * u;
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}
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}
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}
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}
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@@ -124,13 +125,22 @@ namespace FluidSim.Components
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PortB.MassFlowRate = _rightSet ? -_fxR_mass * _area : 0.0;
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PortB.MassFlowRate = _rightSet ? -_fxR_mass * _area : 0.0;
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// Enthalpy for upwinding
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// Enthalpy for upwinding
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PortA.SpecificEnthalpy = _gamma / (_gamma - 1.0) * Pressure(0) / Math.Max(_rho[0], 1e-12);
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PortA.SpecificEnthalpy = GetCellTotalSpecificEnthalpy(0);
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PortB.SpecificEnthalpy = _gamma / (_gamma - 1.0) * Pressure(_n - 1) / Math.Max(_rho[_n - 1], 1e-12);
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PortB.SpecificEnthalpy = GetCellTotalSpecificEnthalpy(_n - 1);
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// Reset for next step
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// Reset for next step
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_leftSet = _rightSet = false;
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_leftSet = _rightSet = false;
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}
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}
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private double GetCellTotalSpecificEnthalpy(int i)
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{
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double rho = Math.Max(_rho[i], 1e-12);
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double u = _rhou[i] / rho;
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double p = Pressure(i);
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double h = _gamma / (_gamma - 1.0) * p / rho;
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return h + 0.5 * u * u;
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}
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double Pressure(int i) =>
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double Pressure(int i) =>
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(_gamma - 1.0) * (_E[i] - 0.5 * _rhou[i] * _rhou[i] / Math.Max(_rho[i], 1e-12));
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(_gamma - 1.0) * (_E[i] - 0.5 * _rhou[i] * _rhou[i] / Math.Max(_rho[i], 1e-12));
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@@ -55,14 +55,19 @@ namespace FluidSim.Core
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bool isLeftBoundary,
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bool isLeftBoundary,
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out double massFlux, out double momFlux, out double energyFlux)
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out double massFlux, out double momFlux, out double energyFlux)
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{
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{
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// mass flow from pipe to volume (positive = pipe → volume)
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// ----- Compute STAGNATION pressures -----
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double mdot = MassFlow(pPipe, rhoPipe, pVol, rhoVol, conn);
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double pStagPipe = pPipe + 0.5 * rhoPipe * uPipe * uPipe;
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double pStagVol = pVol + 0.5 * rhoVol * uVol * uVol; // uVol is always 0 for your volumes
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// Mass flow driven by stagnation pressure difference (positive = pipe→volume)
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double mdot = MassFlow(pStagPipe, rhoPipe, pStagVol, rhoVol, conn);
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// Limit mass flow to the amount that can leave/enter the pipe cell
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// Limit mass flow to the amount that can leave/enter the pipe cell
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double maxMdot = rhoPipe * pipeArea * 343.0;
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double maxMdot = rhoPipe * pipeArea * 343.0;
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if (Math.Abs(mdot) > maxMdot) mdot = Math.Sign(mdot) * maxMdot;
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if (Math.Abs(mdot) > maxMdot) mdot = Math.Sign(mdot) * maxMdot;
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bool flowLeavesPipe = mdot > 0;
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bool flowLeavesPipe = mdot > 0; // pipe → volume
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double uFace, pFace, rhoFace;
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double uFace, pFace, rhoFace;
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double massFluxPerArea;
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double massFluxPerArea;
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@@ -83,7 +88,7 @@ namespace FluidSim.Core
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{ uFace = uVol; pFace = pVol; rhoFace = rhoVol; }
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{ uFace = uVol; pFace = pVol; rhoFace = rhoVol; }
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}
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}
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// Total enthalpy of the injected fluid (corrected: mass flux × total enthalpy)
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// Total enthalpy of the injected fluid
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double specificEnthalpy = (1.4 / (1.4 - 1.0)) * pFace / Math.Max(rhoFace, 1e-12);
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double specificEnthalpy = (1.4 / (1.4 - 1.0)) * pFace / Math.Max(rhoFace, 1e-12);
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double totalEnthalpy = specificEnthalpy + 0.5 * uFace * uFace;
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double totalEnthalpy = specificEnthalpy + 0.5 * uFace * uFace;
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@@ -6,58 +6,46 @@ namespace FluidSim.Core
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{
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{
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public static class Simulation
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public static class Simulation
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{
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{
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private static Solver solver;
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private static Volume0D volA, volB;
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private static Pipe1D pipe;
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private static Pipe1D pipe;
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private static Connection leftConn, rightConn; // dummy connections for orifice params
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private static Connection connA, connB;
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private static int stepCount;
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private static double time;
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private static double time;
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private static double dt;
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private static double dt;
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private static int stepCount;
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public static void Initialize(int sampleRate)
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public static void Initialize(int sampleRate)
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{
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{
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dt = 1.0 / sampleRate;
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dt = 1.0 / sampleRate;
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double V = 5.0 * Units.L;
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volA = new Volume0D(V, 1.1 * Units.atm, Units.Celsius(20), sampleRate);
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volB = new Volume0D(V, 1.0 * Units.atm, Units.Celsius(20), sampleRate);
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double length = 150 * Units.mm;
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double length = 150 * Units.mm;
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double diameter = 25 * Units.mm;
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double diameter = 25 * Units.mm;
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double area = Units.AreaFromDiameter(25, Units.mm);
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double area = Units.AreaFromDiameter(25, Units.mm);
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int nCells = 10;
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int nCells = 10;
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pipe = new Pipe1D(length, area, nCells, sampleRate);
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pipe = new Pipe1D(length, area, nCells, sampleRate);
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pipe.SetUniformState(1.2, 0.0, 1.0 * Units.atm); // start at 1 atm
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pipe.SetUniformState(volA.Density, 0.0, volA.Pressure);
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pipe.FrictionFactor = 0.02;
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pipe.FrictionFactor = 0.02;
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// Dummy connections – only used for orifice parameters
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// Connections with orifice area equal to pipe area (flange joint)
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leftConn = new Connection(null, null) { Area = area, DischargeCoefficient = 1.0, Gamma = 1.4 };
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connA = new Connection(volA.Port, pipe.PortA) { Area = area, DischargeCoefficient = 1.0, Gamma = 1.4 };
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rightConn = new Connection(null, null) { Area = area, DischargeCoefficient = 1.0, Gamma = 1.4 };
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connB = new Connection(pipe.PortB, volB.Port) { Area = area, DischargeCoefficient = 1.0, Gamma = 1.4 };
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solver = new Solver();
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solver.AddVolume(volA);
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solver.AddVolume(volB);
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solver.AddPipe(pipe);
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solver.AddConnection(connA);
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solver.AddConnection(connB);
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}
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}
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public static float Process()
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public static float Process()
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{
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{
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// Fixed boundary reservoirs
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solver.Step();
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double pLeft = 1.1 * Units.atm;
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double rhoLeft = 1.2;
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double uLeft = 0.0;
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double pRight = 1.0 * Units.atm;
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double rhoRight = 1.2;
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double uRight = 0.0;
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// Compute boundary fluxes via orifice model
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OrificeBoundary.PipeVolumeFlux(
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pipe.GetLeftPressure(), pipe.GetLeftDensity(), 0.0,
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pLeft, rhoLeft, uLeft,
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leftConn, pipe.Area, true,
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out double leftMassFlux, out double leftMomFlux, out double leftEnergyFlux);
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OrificeBoundary.PipeVolumeFlux(
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pipe.GetRightPressure(), pipe.GetRightDensity(), 0.0,
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pRight, rhoRight, uRight,
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rightConn, pipe.Area, false,
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out double rightMassFlux, out double rightMomFlux, out double rightEnergyFlux);
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pipe.SetLeftBoundaryFlux(leftMassFlux, leftMomFlux, leftEnergyFlux);
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pipe.SetRightBoundaryFlux(rightMassFlux, rightMomFlux, rightEnergyFlux);
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pipe.Simulate();
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time += dt;
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time += dt;
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stepCount++;
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stepCount++;
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Log();
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Log();
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@@ -66,20 +54,13 @@ namespace FluidSim.Core
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public static void Log()
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public static void Log()
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{
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{
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if (stepCount <= 20 || stepCount % 50 == 0)
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if (stepCount <= 50 || stepCount % 200 == 0)
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{
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{
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Console.WriteLine($"Step {stepCount:D4} t = {time * 1e3:F3} ms");
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Console.WriteLine(
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for (int i = 0; i < pipe.GetCellCount(); i++)
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$"t = {time * 1e3:F3} ms Step {stepCount:D4}: " +
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{
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$"PA = {volA.Pressure / 1e5:F6} bar, " +
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double rho = pipe.GetCellDensity(i);
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$"PB = {volB.Pressure / 1e5:F6} bar, " +
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double p = pipe.GetCellPressure(i);
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$"FlowA = {pipe.PortA.MassFlowRate * 1e3:F2} g/s");
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double u = pipe.GetCellVelocity(i);
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Console.WriteLine($" Cell {i}: ρ={rho:F4} kg/m³ p={p / 1e5:F6} bar u={u:F3} m/s");
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}
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double leftFlow = pipe.PortA.MassFlowRate;
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double rightFlow = pipe.PortB.MassFlowRate;
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Console.WriteLine($" Left flow = {leftFlow * 1e3:F4} g/s Right flow = {rightFlow * 1e3:F4} g/s");
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Console.WriteLine();
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}
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}
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}
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}
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}
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}
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@@ -20,7 +20,7 @@ namespace FluidSim.Core
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foreach (var v in _volumes)
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foreach (var v in _volumes)
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v.PushStateToPort();
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v.PushStateToPort();
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// 2. Apply orifice boundaries to pipes
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// 2. Compute boundary fluxes (orifice model)
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foreach (var conn in _connections)
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foreach (var conn in _connections)
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{
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{
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if (IsPipePort(conn.PortA) && IsVolumePort(conn.PortB))
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if (IsPipePort(conn.PortA) && IsVolumePort(conn.PortB))
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@@ -31,20 +31,20 @@ namespace FluidSim.Core
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VolumeToVolume(conn);
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VolumeToVolume(conn);
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}
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}
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// 3. Pipes simulate
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// 3. Pipe simulation step
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foreach (var p in _pipes)
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foreach (var p in _pipes)
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p.Simulate();
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p.Simulate();
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// 4. Transfer pipe flows to connected volumes
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// 4. Transfer pipe‑port data to volumes
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foreach (var conn in _connections)
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foreach (var conn in _connections)
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{
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{
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if (IsPipePort(conn.PortA) && IsVolumePort(conn.PortB))
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if (IsPipePort(conn.PortA) && IsVolumePort(conn.PortB))
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Transfer(conn.PortA, conn.PortB);
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TransferPipeToVolume(conn.PortA, conn.PortB);
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else if (IsVolumePort(conn.PortA) && IsPipePort(conn.PortB))
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else if (IsVolumePort(conn.PortA) && IsPipePort(conn.PortB))
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Transfer(conn.PortB, conn.PortA);
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TransferPipeToVolume(conn.PortB, conn.PortA);
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}
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}
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// 5. Volumes integrate
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// 5. Integrate volumes
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foreach (var v in _volumes)
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foreach (var v in _volumes)
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v.Integrate();
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v.Integrate();
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}
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}
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@@ -61,34 +61,56 @@ namespace FluidSim.Core
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double pP = isLeft ? pipe.GetLeftPressure() : pipe.GetRightPressure();
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double pP = isLeft ? pipe.GetLeftPressure() : pipe.GetRightPressure();
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double rhoP = isLeft ? pipe.GetLeftDensity() : pipe.GetRightDensity();
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double rhoP = isLeft ? pipe.GetLeftDensity() : pipe.GetRightDensity();
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double uP = 0.0;
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double uP = isLeft ? pipe.GetCellVelocity(0)
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double pV = volPort.Pressure, rhoV = volPort.Density, uV = 0.0;
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: pipe.GetCellVelocity(pipe.GetCellCount() - 1);
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double pV = volPort.Pressure;
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double rhoV = volPort.Density;
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double uV = 0.0; // volume has zero organized velocity
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OrificeBoundary.PipeVolumeFlux(
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pP, rhoP, uP,
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pV, rhoV, uV,
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conn, pipe.Area, isLeft,
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out double massFlux, out double momFlux, out double energyFlux);
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OrificeBoundary.PipeVolumeFlux(pP, rhoP, uP, pV, rhoV, uV, conn, pipe.Area,
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isLeft, out double mf, out double pf, out double ef);
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if (isLeft)
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if (isLeft)
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pipe.SetLeftBoundaryFlux(mf, pf, ef);
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pipe.SetLeftBoundaryFlux(massFlux, momFlux, energyFlux);
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else
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else
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pipe.SetRightBoundaryFlux(mf, pf, ef);
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pipe.SetRightBoundaryFlux(massFlux, momFlux, energyFlux);
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}
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}
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void VolumeToVolume(Connection conn)
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void VolumeToVolume(Connection conn)
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{
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{
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double mdot = OrificeBoundary.MassFlow(conn.PortA.Pressure, conn.PortA.Density,
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double mdot = OrificeBoundary.MassFlow(
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conn.PortB.Pressure, conn.PortB.Density, conn);
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conn.PortA.Pressure, conn.PortA.Density,
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conn.PortB.Pressure, conn.PortB.Density, conn);
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conn.PortA.MassFlowRate = -mdot;
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conn.PortA.MassFlowRate = -mdot;
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conn.PortB.MassFlowRate = mdot;
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conn.PortB.MassFlowRate = mdot;
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if (mdot > 0)
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if (mdot > 0)
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conn.PortB.SpecificEnthalpy = conn.PortA.SpecificEnthalpy;
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conn.PortB.SpecificEnthalpy = conn.PortA.SpecificEnthalpy;
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else if (mdot < 0)
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else if (mdot < 0)
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conn.PortA.SpecificEnthalpy = conn.PortB.SpecificEnthalpy;
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conn.PortA.SpecificEnthalpy = conn.PortB.SpecificEnthalpy;
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}
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}
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void Transfer(Port pipePort, Port volPort)
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void TransferPipeToVolume(Port pipePort, Port volPort)
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{
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{
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double mdot = pipePort.MassFlowRate;
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double mdot = pipePort.MassFlowRate;
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// mdot > 0 → fluid enters pipe from volume
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// mdot < 0 → fluid leaves pipe and enters volume
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// Volume mass flow sign is opposite (positive into volume)
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volPort.MassFlowRate = -mdot;
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volPort.MassFlowRate = -mdot;
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volPort.SpecificEnthalpy = pipePort.SpecificEnthalpy;
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if (mdot < 0) // pipe → volume
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{
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// ★ pipePort.SpecificEnthalpy now contains TOTAL enthalpy
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volPort.SpecificEnthalpy = pipePort.SpecificEnthalpy;
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}
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// else: fluid goes volume → pipe → volume owns its own (static) enthalpy,
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// which is already correct.
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}
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}
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}
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}
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}
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}
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@@ -1,10 +0,0 @@
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using System;
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using System.Collections.Generic;
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using System.Text;
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namespace FluidSim.Interfaces
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{
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internal class Junction0
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{
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}
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}
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@@ -1,10 +0,0 @@
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using System;
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using System.Collections.Generic;
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using System.Text;
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namespace FluidSim.Interfaces
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{
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internal class Junction1
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{
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}
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}
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Reference in New Issue
Block a user