| Gravity or API-Type Separator | Approximately 1–1,000 m³/h | Free-floating and settleable oil droplets, generally larger than 150 microns | Approximately 50–90%, depending on detention time, temperature, and inlet conditions | Typically 50–150 mg/L after primary separation | Large footprint; usually installed as an in-ground or above-ground tank with inlet and outlet control | Remove accumulated oil and settled solids regularly; inspect baffles, skimmers, sludge zones, and access covers at least monthly | High-flow industrial wastewater, stormwater, workshops, garages, and preliminary treatment |
| Coalescing Plate Separator | Approximately 1–500 m³/h | Free oil and dispersed oil droplets that can merge on inclined coalescing media | Approximately 85–99% for properly designed free-oil loads | Typically 5–50 mg/L, depending on influent quality and droplet size | More compact than a basic gravity separator; requires sufficient access for media removal or cleaning | Clean coalescing plates when differential pressure rises or flow decreases; remove separated oil and sludge; inspect quarterly under normal service | Vehicle maintenance facilities, equipment yards, manufacturing plants, and commercial wash-water systems |
| Centrifugal Separator | Approximately 0.5–100 m³/h per unit | Free and dispersed oil, suspended solids, and some fine droplets under controlled loading | Approximately 80–98%; performance depends strongly on density difference and feed consistency | Typically 10–75 mg/L after one treatment stage | Compact and suitable where floor space is limited; often requires a pump, controls, and stable feed pressure | Inspect rotating or internal components, check seals and bearings, remove collected solids, and follow scheduled lubrication or replacement intervals | Compact industrial systems, metalworking fluids, process-water recycling, and sites with limited space |
| Hydrocyclone Oil Separator | Approximately 1–200 m³/h per unit | Free and dispersed oil where there is adequate density difference between oil and water | Approximately 70–95% for suitable feed conditions; less effective for stable emulsions | Typically 20–100 mg/L, depending on inlet concentration and droplet distribution | Very compact with no moving parts; normally requires a pump and a reliable pressure differential | Flush the unit, inspect the apex and vortex finder, monitor pressure drop, and prevent abrasive solids from causing wear | Offshore and marine applications, produced-water pre-treatment, and compact process installations |
| Centrifuge or Disc-Stack Separator | Approximately 0.1–50 m³/h per unit | Fine suspended solids and dispersed oil, including smaller droplets than gravity systems can remove | Approximately 90–99% for suitable feed conditions and correctly selected equipment | Typically 5–30 mg/L after optimized operation | Small footprint but higher electrical, control, and installation requirements; may need pre-screening | Frequent inspection and cleaning; maintain bearings, seals, solids discharge mechanisms, and vibration levels according to the operating schedule | High-value water reuse, industrial process water, refineries, and applications requiring consistent effluent quality |
| Dissolved Air Flotation System | Approximately 5–500 m³/h | Fine dispersed oil, emulsified oil after conditioning, suspended solids, and flocculated contaminants | Approximately 90–99% when chemical conditioning and air saturation are properly controlled | Typically 5–30 mg/L; actual results depend on emulsion stability and chemical selection | Moderate to large footprint; requires a recycle pump, air system, skimmer, and usually chemical storage and dosing equipment | Skim floated sludge, clean nozzles and saturator components, calibrate chemical dosing, inspect pumps, and monitor air and recycle pressure daily | Food processing, refineries, chemical manufacturing, oily wastewater with stable emulsions, and strict discharge limits |