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Case Study: Offshore Produced Water Treatment — OSPAR Compliance

A North Sea oil production platform was generating 8,000 m³/day of produced water with oil-in-water concentrations exceeding the OSPAR 30 mg/L discharge limit. Reynolds & Bauhm designed a compact skid-mounted treatment system for platform installation.

Oil & GasOffshoreProduced WaterDAFOSPAR ComplianceNorth Sea
<10 mg/LOil in Water
8,000 m³/dayProduced Water
30%Footprint vs. Alternatives
OSPARCompliant

The Challenge

The platform was producing oil from a maturing reservoir with increasing water-cut. Produced water volume had grown from 2,000 to 8,000 m³/day over 4 years, exceeding the capacity of existing hydrocyclone separators. Oil-in-water at the overboard discharge point was consistently 45–85 mg/L — above the OSPAR Convention 30 mg/L limit (instantaneous) and 40 mg/L monthly average.

  • Produced water composition: oil 50–120 mg/L; iron 15–40 mg/L; dissolved organics (BTEX) 3–12 mg/L; H&sub2;S 2–8 mg/L; TDS 35,000–50,000 mg/L
  • Platform constraints: weight budget <45 tonnes; footprint <30 m²; ATEX Zone 1 classification; process operated at 70°C inlet temperature
  • Regulatory deadline: OSPAR authority enforcement notice; 6-month compliance window
  • Existing hydrocyclones retained as primary separation — new system to treat hydrocyclone overflow only

The Solution

Reynolds & Bauhm designed a compact, ATEX-certified skid combining induced gas flotation and walnut-shell media filtration, meeting the platform weight and footprint constraints:

  • Induced gas flotation (IGF) using produced gas rather than air — ATEX-safe, no air ingress risk; residence time 3 minutes; internal paddle skimmer removes float oil to slop system
  • Dual walnut-shell pressure filters operating alternately, each 6 m² vessel; backwash with produced water; cake returned to produced water header for reprocessing
  • Chemical dosing: de-emulsifier at 20–50 mg/L ahead of IGF; low-shear injection to avoid re-emulsification
  • SCADA integration: oil-in-water analyser (UV fluorescence) controls de-emulsifier dosing automatically and triggers filter backwash at <7 mg/L effluent oil; see our SCADA services
  • Entire system factory-tested and ATEX-certified before offshore installation; offshore installation completed in 14 days during scheduled shutdown

Process Train

StageEquipmentPerformance
1Existing hydrocyclone separators (retained)Oil reduced from 120 to 50–80 mg/L
2De-emulsifier dosing (produced gas injection)Droplet coalescence; d50 >30 µm
3Induced gas flotation (3-cell series)Oil 80 → 15–20 mg/L
4Walnut-shell media filter (duty/standby)Oil 20 → <10 mg/L; iron <2 mg/L
5UV fluorescence oil-in-water analyserContinuous compliance monitoring; OSPAR data logging
6Overboard discharge or reinjectionOSPAR compliant at <10 mg/L OIW

Results Achieved

OSPAR Compliance

Oil-in-water at discharge consistently <10 mg/L — three times below the 30 mg/L limit. Zero exceedances in first 18 months of operation. Enforcement notice withdrawn.

Platform Fit

Total system weight: 38 tonnes ( 45 tonnes). Footprint: 24 m² ( 30 m²). Installed during 14-day scheduled shutdown with no production interruption.

Automated Operation

System operates with zero additional operator attendance above existing duties. Automated backwash and dosing control confirmed by 6-month unattended performance review.

Remote Monitoring & Diagnostics

SCADA-linked instrumentation transmits performance data to shore-based engineers, enabling predictive maintenance and rapid troubleshooting without offshore visits.

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