orifice_flow_iso5167
Calculate mass flow through an orifice plate per ISO 5167-2 using the Reader-Harris/Gallagher discharge coefficient equation, solved iteratively against pipe Reynolds number. Supports corner, flange and D&D/2 taps, gas expansibility and permanent pressure loss. Powered by multicalci.com.
Input Schema
| Name | Required | Description | Default |
|---|---|---|---|
| tap_type | No | Pressure tap arrangement | flange |
| pipe_id_mm | Yes | Pipe internal diameter D, mm | |
| fluid_state | No | Fluid state; gas/steam applies expansibility | liquid |
| density_kgm3 | No | Upstream fluid density, kg/m3 | |
| viscosity_cp | No | Dynamic viscosity, cP | |
| orifice_bore_mm | Yes | Orifice bore diameter d at flowing temperature, mm | |
| isentropic_exponent | No | Isentropic exponent kappa (gas/steam only) | |
| upstream_pressure_bara | No | Upstream static pressure, bar a (gas/steam only) | |
| differential_pressure_pa | Yes | Measured differential pressure, Pa | |
| downstream_pressure_bara | No | Downstream static pressure, bar a (gas/steam only) |