Given the inlet flow (Q), the upstream and throat diameters (D1, D2), and the upstream piezometric head (P1/γ), this computes the velocity heads at sections 1 and 2, the piezometric heads at the throat (P2/γ) and downstream (P3/γ), and the head losses in the nozzle (hf¹²) and diffuser (hf¹³).
Assumptions: steady, incompressible flow, same elevation reference (no elevation terms), empirical correlations for nozzle and diffuser losses.
Venturi
$$ \begin{aligned} A_1 &= \frac{\pi D_1^2}{4}, \quad A_2 = \frac{\pi D_2^2}{4} \ U_1 &= \frac{Q}{A_1}, \quad U_2 = \frac{Q}{A_2} \ h_f^{12} &= 0.15,\frac{U_2^2}{2g} \ h_f^{13} &= 2.5,\frac{U_2^2}{2g} \ \frac{P_2}{\gamma} &= \frac{P_1}{\gamma} + \frac{U_1^2}{2g} - \frac{U_2^2}{2g} - h_f^{12} \ \frac{P_3}{\gamma} &= \frac{P_1}{\gamma} - h_f^{13} \end{aligned} $$
Default input units: Q in L/s, D1 and D2 in mm; heads in m.
Parameter | Default units | Description |
|---|---|---|
Flow | L/s | Inlet flow rate (Q) |
Upstream diameter | mm | Pipe inside diameter upstream (D1) |
Throat diameter | mm | Venturi throat diameter (D2) |
P¹/γ | m | Upstream piezometric head (P1/γ) |
Parameter | Default units | Description |
|---|---|---|
U1²/2g | m | Velocity head at section 1 (U1²/2g) |
U2²/2g | m | Velocity head at throat (U2²/2g) |
hf¹² | m | Nozzle head loss (1→2) |
hf¹³ | m | Diffuser head loss (1→3) |
P²/γ | m | Piezometric head at throat (P2/γ) |
P³/γ | m | Piezometric head downstream (P3/γ) |
Flow | L/s | Output flow (same as input), Qout = Q |