Professional Bernoulli Equation Solver

This professional-grade calculator solves the complete Bernoulli Energy Equation for steady, incompressible fluid flow with optional friction loss corrections. Determines unknown parameter (Pressure, Velocity, or Height) at point 2 with advanced capabilities including temperature-dependent fluid properties, energy loss coefficients, and industrial application support.

Key Features: Supports water, oil, and gas with temperature interpolation; optional friction/minor loss accounting; pressure/velocity/height solvers; comprehensive calculation transparency; PDF export for engineering documentation; and professional-grade accuracy per ISO and fundamental fluid mechanics standards.

Bernoulli Equation: \(P_1 + \rho g h_1 + \frac{1}{2}\rho v_1^2 + \text{(losses)}_{12} = P_2 + \rho g h_2 + \frac{1}{2}\rho v_2^2\)

Calculation Configuration

Fluid Properties

Point 1 (Reference) Parameters

Point 2 (Solution) Parameters

Bernoulli Analysis Results

Parameter Value

Advanced Bernoulli Equation Theory & Applications

Energy Equation Fundamentals

Bernoulli's equation represents conservation of mechanical energy along a streamline for steady, incompressible flow of an inviscid (frictionless) fluid. The equation balances three forms of energy: pressure head (P/ρg), velocity head (v²/2g), and elevation head (h). For real fluids with friction, the equation is modified by adding energy loss terms (friction losses and minor losses).

Temperature Effects on Fluid Properties

Fluid density varies significantly with temperature. Water density changes from ~1000 kg/m³ at 0°C to ~958 kg/m³ at 100°C. Oil viscosity and density also vary substantially. Air density follows ideal gas law inversely proportional to absolute temperature. Accurate temperature-corrected properties are essential for precision calculations in thermal systems, heat exchangers, and cryogenic applications.

Friction and Minor Loss Corrections

Real flows experience energy losses from wall friction (major losses) and fittings/expansions/contractions (minor losses). Major losses follow Darcy-Weisbach: hf = f(L/D)(v²/2g). Minor losses use: hm = K(v²/2g) where K depends on fitting type. Total loss = hf + hm. Proper accounting for losses is critical in pump sizing, system pressure drop analysis, and industrial flow measurement.

Industrial Applications

Siphon Design: Determines maximum height and priming requirements. Jet Propulsion: Calculates nozzle exit velocity and thrust. Pipe Networks: Analyzes pressure distribution and flow split. Hydroturbines: Determines available head and power output. Heat Exchangers: Balances pressure drops and flow distribution. Pumping Systems: Verifies pump discharge head requirements.

Practical Design Considerations

Bernoulli assumes inviscid flow; real applications require viscous corrections. Reynolds number determines viscous effects: Re < 1000 requires significant correction, while Re > 10000 approaches ideal behavior. Turbulent kinetic energy and pressure fluctuations add complexity. For compressible flow (gases), additional density corrections apply. Always verify calculations against experimental data and include appropriate safety factors.