🌀 Bernoulli & Extended Energy Equation Calculator
Solve fluid energy balances across pipelines. Model simple inviscid systems or extended energy lines incorporating pipe size changes, pumps, turbines, and friction losses.
Conservation of Energy in Pipes
The Bernoulli and Extended Energy equations govern the balance of pressure head, velocity head, and elevation head in a flowing fluid system. Real pipelines lose energy due to wall friction and components ($h_L$), and can gain or lose energy via mechanical pumps ($h_p$) and turbines ($h_t$).
• Hydraulic Grade Line (HGL): Represents the sum of static pressure and elevation heads ($H - V^2/2g$).
• Continuity: Decreasing the pipe diameter increases the velocity head at the cost of static pressure head.
📝 Configuration
📊 Results & Grade Lines
Configure inputs and click Calculate Fluid Energy to view results.
📘 Calculation Methodology
Mathematical Model & Theory
The conservation of mechanical energy along a streamline in steady, incompressible, one-dimensional flow is described by the **Extended Energy Equation**:
Where each term represents energy per unit weight (head, in meters):
- Pressure Head ($P/\rho g$): Height of fluid column corresponding to static pressure.
- Velocity Head ($V^2/2g$): Kinetic energy of the fluid per unit weight.
- Elevation Head ($z$): Potential energy due to height above an arbitrary datum.
- Pump Head ($h_{pump}$): Energy head added by mechanical pumps.
- Turbine Head ($h_{turb}$): Energy head extracted by turbines.
- Head Loss ($h_L$): Energy dissipated due to friction and fittings.
Academic References
- Munson, B. R., Young, D. F., & Okiishi, T. H.: Fundamentals of Fluid Mechanics, John Wiley & Sons.
- Cengel, Y. A., & Cimbala, J. M.: Fluid Mechanics: Fundamentals and Applications, McGraw-Hill, Ch. 5.
Worked Engineering Example
A pump lifts water ($\rho = 1000\text{ kg/m}^3$) from an open reservoir at $z_1 = 0\text{ m}$ to a tank at $z_2 = 15\text{ m}$ and $P_2 = 150\text{ kPa}$. The velocities are negligible at the reservoir surface and $V_2 = 2.0\text{ m/s}$ at the outlet. Pipe friction head loss is $h_L = 3.5\text{ m}$. Calculate the required pump head ($h_{pump}$).
Step-by-step Solution:
1. Apply energy equation ($P_1=0$, $V_1=0$, $h_{turb}=0$):
$$0 + 0 + z_1 + h_{pump} = \frac{P_2}{\rho g} + \frac{V_2^2}{2g} + z_2 + h_L$$ 2. Calculate heads:
- Pressure head: $\frac{150,000}{1000 \times 9.81} = 15.29\text{ m}$
- Velocity head: $\frac{2.0^2}{2 \times 9.81} = 0.20\text{ m}$
3. Solve for $h_{pump}$:
$$h_{pump} = 15.29 + 0.20 + (15 - 0) + 3.5 = 33.99\text{ m}$$
Final Result:
The pump must add 33.99 meters of head to lift the water.