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Featured Projects

Desalter wastewater (Untreated (L); 1st Treatment Stage (M); 2nd Treatment Stage (R)).

Desalter wastewater (Untreated (L); 1st Treatment Stage (M); 2nd Treatment Stage (R)).

Refinery Desalter Wastewater 2 stage Electrochemical treatment project. Started in the United States in 2024. Process flow rate: 20-100 gpm.

Contaminant Reduction
  • Oil/Grease: 99.6%
  • Sulfide: 92%
  • TKN: 25%
  • TSS: 90%
  • COD: 80%
  • Ammonia: 100%
Food Processing (Untreated (L), Treated (R)).

Food Processing (Untreated (L), Treated (R)).

25 gpm batch pet food facility. Project started in the United States.

Contaminant Reduction
  • Oil/Grease: 100%
  • TSS: 98%
  • COD: 74%
Flowback and Production water storage.

Flowback and Production water storage.

Vehicle parts manufacturing facility in the United States. 20 gpm process flow rate.

Contaminant Reduction
  • Oil/Grease: 100%
  • Iron: 99%
  • Sulfide: 95%
  • TSS: 90%

Increase with Electro-Oxidation:ORP: from 13 mV in the untreated to 900+ mV in the Electro-Oxidation treated sample.

Plating Facility (Untreated (L), Treated (R)).

Plating Facility (Untreated (L), Treated (R)).

United States plating facility project; 10 gpm process.

Contaminant Reduction
  • Oil/Grease: 100%
  • TSS: 59%
  • COD: 16%
  • Barium: 100%
  • Chromium: 99.5%
  • Lead: 100%
  • Nickel: 99%
  • Silver: 100%

Recent Projects

Production Water (Untreated (L); Treated (R)).

Production Water (Untreated (L); Treated (R)).

Contaminant Reduction
  • ORP >700 mV
  • Iron: 100%
  • Barium: 33%
  • Calcium: 37%
  • Total Suspended Solids: 63%
  • Volatile Organic Compounds: up to 100%
  • Volatile Petroleum Hydrocarbons: >87%
  • Semi-Volatile Petroleum Hydrocarbons: up to 60%
Production Water (Untreated (L); Treated (R)).

Production Water (Untreated (L); Treated (R)).

Contaminant Reduction
  • ORP > +999 (Over Range)
  • Iron: 92%
  • Total Suspended Solids: 94%
  • Volatile Organic Compounds: up to 97%
  • Volatile Petroleum Hydrocarbons: >81%
  • Semi-Volatile Petroleum Hydrocarbons: up to 68%
3 Well Flowback Water (Untreated (L); Treated (R)).

3 Well Flowback Water (Untreated (L); Treated (R)).

Contaminant Reduction
  • ORP 938 mV
  • Iron: 94%
  • Barium: 69%
  • Total Suspended Solids: 40%
  • Volatile Organic Compounds: up to 97%
  • Volatile Petroleum Hydrocarbons: >97%
  • Semi-Volatile Petroleum Hydrocarbons: >98%
Plating (Untreated (L); Treated (R)).

Plating (Untreated (L); Treated (R)).

Contaminant Reduction
  • Chrome: 100%
  • Copper: 96%
  • Iron: 62%
  • Nickel: 50%
  • Phosphorus: 98%
  • Lead: 80%
  • Zn: 100%
  • Oil/Grease: 100%
Plating Facility (Untreated (L), Treated (R)).

Plating Facility (Untreated (L), Treated (R)).

Contaminant Reduction
  • Oil/Grease: 100%
  • TSS: 59%
  • COD: 16%
  • Barium: 100%
  • Chromium: 99.5%
  • Lead: 100%
  • Nickel: 99%
  • Silver: 100%
Seafood Processing.

Seafood Processing.

Contaminant Reduction
  • Oil/Grease: 70%
  • Phosphorous: 98%
  • COD: 51%
  • Nitrogen: 62%
  • Ammonia: 95%
  • TKN: 75%
  • TSS: 99%
  • BOD: 77%
  • TOC: 39%
Food Processing (Untreated (L), Treated (R)).

Food Processing (Untreated (L), Treated (R)).

Contaminant Reduction
  • Oil/Grease: 100%
  • TSS: 98%
  • COD: 74%
Desalter wastewater (Untreated (L); 1st Treatment Stage (M); 2nd Treatment Stage (R)).

Desalter wastewater (Untreated (L); 1st Treatment Stage (M); 2nd Treatment Stage (R)).

Contaminant Reduction
  • Oil/Grease: 99.6%
  • Sulfide: 92%
  • TKN: 25%
  • TSS: 90%
  • COD: 80%
  • Ammonia: 100%
Flowback and Production water storage.

Flowback and Production water storage.

Contaminant Reduction
  • Oil/Grease: 100%
  • Iron: 99%
  • Sulfide: 95%
  • TSS: 90%

Increase with Electro-Oxidation:ORP: from 13 mV in the untreated to 900+ mV in the Electro-Oxidation treated sample.

Rich Amine Recovery (Untreated (L); Treated (R)).

Rich Amine Recovery (Untreated (L); Treated (R)).

Contaminant Reduction
  • Total Suspended Solids
  • Iron
  • Aluminum