Design an API 421 oil–water separator (rectangular gravity separator) by estimating the oil droplet rise velocity (Stokes’ law), defining a conservative horizontal velocity, and sizing the cross-sectional area, number of channels, channel depth, and separator length, according to API 421 hydraulic and geometric recommendations.
API 421 oil–water separator
Oil droplet rise (terminal) velocity (Stokes regime):
Where:
The calculation assumes a fixed design droplet diameter:
A preliminary horizontal velocity is defined as:
This velocity is then limited to a maximum of 3 ft/min, following API-style conservative practice. The resulting value vh is used for all subsequent calculations.
Cross-sectional flow area:
Number of channels (each channel limited to 160 ft²):
Channel depth:
Separator length:
Velocity ratio:
Turbulence factor F obtained by linear interpolation from API 421:
| R | 3 | 6 | 10 | 15 | 20 |
|---|---|---|---|---|---|
| F | 1.28 | 1.37 | 1.52 | 1.64 | 1.74 |
Warnings are issued when values fall outside API 421 typical guidance:
| Parameter | Default units | Description |
|---|---|---|
| Flow rate (Q) | m³/s | Wastewater volumetric flow rate through the separator. |
| Water viscosity (μ) | Pa·s | Dynamic viscosity of the water phase (default 0.001 Pa·s). |
| Water density (ρw) | kg/m³ | Density of water (default 1000 kg/m³). |
| Oil density (ρo) | kg/m³ | Density of oil (default 900 kg/m³). |
| Channel width (B) | ft | Width of each separator channel (default 10 ft). |
| Parameter | Default units | Description |
|---|---|---|
| Oil droplet rise rate (vt) | ft/s | Terminal rise velocity of oil droplets. |
| Horizontal velocity (vh) | ft/s | Adopted average horizontal flow velocity. |
| Cross-sectional area (Ac) | ft² | Required separator cross-sectional area. |
| Channel depth (d) | ft | Depth of each separator channel. |
| Separator length (L) | ft | Required separator length. |
| Number of channels (n) | – | Number of parallel separator channels. |