Last Updated: July 2026 | Reading Time: 13 minutes
What is COD?
Chemical Oxygen Demand (COD) is a measure of the total amount of oxygen required to oxidize all organic and oxidizable inorganic compounds in water. Unlike BOD (Biochemical Oxygen Demand), which measures only biologically degradable organic matter, COD measures all oxidizable substances, making it a more comprehensive indicator of water pollution.
High COD levels indicate high organic pollution, which depletes dissolved oxygen in receiving waters and harms aquatic ecosystems. Strict discharge limits for COD are enforced in most countries.
COD Removal Methods Overview
There are multiple approaches to COD removal, each with different mechanisms, costs, and effectiveness. The choice of method depends on COD concentration, effluent composition, discharge standards, and operational budget.
| Method Category | Typical COD Removal | Capital Cost | Operating Cost | Best For |
|---|---|---|---|---|
| Physical-Chemical (Coagulation) | 30 – 60% | Low-Medium | Medium | Suspended and colloidal COD |
| Biological (Aerobic) | 70 – 95% | Medium | Low-Medium | Biodegradable organic COD |
| Biological (Anaerobic) | 60 – 90% | High | Low | High COD (>3,000 mg/L) |
| Advanced Oxidation (AOPs) | 50 – 95% | Medium-High | High | Refractory/non-biodegradable COD |
| Adsorption (Activated Carbon) | 20 – 80% | Low-Medium | High | Polishing, residual COD |
| Membrane Filtration | 30 – 99% | High | High | High-quality effluent requirements |
1. Physical-Chemical Treatment (Coagulation-Flocculation)
How It Works
Coagulation uses metal salts to destabilize colloidal particles and dissolved organic matter, forming flocs that can be separated by sedimentation or flotation. This method primarily removes suspended and colloidal COD, but can also remove some dissolved organic compounds through adsorption onto metal hydroxide flocs.
Common Coagulants for COD Removal
| Coagulant | COD Removal Efficiency | Optimal pH | Sludge Volume |
|---|---|---|---|
| PAC (Poly Aluminium Chloride) | 30 – 55% | 5.5 – 8.0 | Low |
| PFS (Poly Ferric Sulfate) | 40 – 60% | 4.5 – 8.0 | Medium |
| Alum (Aluminum Sulfate) | 25 – 50% | 5.5 – 7.5 | High |
| Ferric Chloride | 35 – 55% | 4.0 – 7.0 | Medium |
| PAC + PFS Blend | 45 – 65% | 5.0 – 7.5 | Medium |
Typical Dosage and Performance
- PAC dosage: 50 – 300 mg/L (30% Al₂O₃ basis)
- PAM (flocculant aid): 0.5 – 5 mg/L (anionic, medium MW)
- Typical COD removal: 40-60% for wastewater with high colloidal content
- Retention time: 10-30 min coagulation, 30-60 min sedimentation
Pros and Cons
Pros: Low capital cost, simple operation, fast results, also removes SS and color
Cons: Limited effectiveness on dissolved COD, produces chemical sludge, ongoing chemical cost
2. Biological Treatment Methods
Aerobic Biological Treatment
Activated Sludge Process
The most common biological COD removal method. Microorganisms break down organic matter in the presence of oxygen, converting it to CO₂, water, and new biomass.
- COD removal: 70 – 95% for biodegradable COD
- HRT: 8 – 48 hours
- MLSS: 2,000 – 5,000 mg/L
- DO requirement: 2 – 4 mg/L
- Best for: Municipal and biodegradable industrial wastewater
MBBR (Moving Bed Biofilm Reactor)
MBBR uses floating plastic carriers with biofilm growth, combining the advantages of activated sludge and biofilm processes.
- COD removal: 75 – 90%
- Advantages: Compact, no sludge bulking, stable operation
- Applications: Industrial wastewater treatment, plant retrofits
MBR (Membrane Bioreactor)
Combines biological treatment with membrane filtration for superior effluent quality.
- COD removal: 90 – 98%
- Effluent quality: Very low SS, can be directly reused
- Disadvantages: High capital cost, membrane fouling management
Anaerobic Biological Treatment
For high-COD wastewater (typically >3,000 mg/L), anaerobic treatment is more cost-effective than aerobic processes.
UASB (Upflow Anaerobic Sludge Blanket)
- COD removal: 60 – 90%
- Applicable COD range: 2,000 – 50,000 mg/L
- Advantages: Low energy, produces biogas (methane), minimal sludge
- Disadvantages: Longer startup, sensitive to toxicants, requires post-treatment
IC Reactor (Internal Circulation)
- COD removal: 70 – 90%
- Higher organic loading rate than UASB (15-30 kg COD/m³/day)
- Best for: High-strength industrial wastewater
Combined Anaerobic + Aerobic Process
For complex industrial wastewater with both high COD and refractory organics, combining anaerobic pretreatment with aerobic polishing achieves the best results:
- Anaerobic stage: removes 60-80% of bulk COD
- Aerobic stage: polishes remaining biodegradable COD
- Chemical tertiary: removes refractory COD
- Total COD removal: 95 – 99%
3. Advanced Oxidation Processes (AOPs)
AOPs generate highly reactive hydroxyl radicals (•OH) that oxidize virtually all organic compounds. These are especially valuable for refractory (non-biodegradable) COD.
Fenton / Fenton-Like Oxidation
Most widely used AOP for industrial wastewater, using ferrous iron as catalyst and hydrogen peroxide as oxidant.
- Mechanism: Fe²⁺ + H₂O₂ → Fe³⁺ + •OH + OH⁻
- COD removal: 50 – 80%
- Optimal pH: 3.0 – 4.0
- Typical H₂O₂ dosage: 0.5 – 2.0 x COD (molar ratio)
- Fe²⁺:H₂O₂ ratio: 1:5 to 1:20 (molar)
- Reaction time: 1 – 4 hours
Pros: Effective for refractory COD, relatively simple equipment, moderate cost
Cons: Requires pH adjustment, produces iron sludge, H₂O₂ cost
Ozone-Based Oxidation (O₃, O₃/H₂O₂, Catalytic Ozonation)
- COD removal: 30 – 70%
- Advantages: No sludge, on-site generation, also disinfects and decolorizes
- Disadvantages: High energy cost, ozone generator capital cost
- Best for: Drinking water, polishing applications, color removal
Electrochemical Oxidation
- COD removal: 40 – 90%
- Advantages: No chemical addition, small footprint, easy automation
- Disadvantages: High energy consumption, electrode cost and fouling
- Best for: Small flow, high-value wastewater
UV-Based AOPs (UV/H₂O₂, UV/O₃, UV/TiO₂)
- COD removal: 40 – 80%
- Advantages: No chemical residue, fast reaction
- Disadvantages: High energy cost, UV lamp replacement
- Best for: Low COD polishing, drinking water treatment
4. Adsorption Methods
Activated Carbon Adsorption
Granular or powdered activated carbon adsorbs organic compounds onto its high-surface-area structure.
- COD removal: 20 – 80% (depends on carbon type and dosage)
- PAC (Powdered Activated Carbon) dosage: 50 – 500 mg/L
- GAC contact time: 10 – 30 minutes
- Best for: Tertiary polishing, low-concentration refractory COD
Pros: Simple to add, broad-spectrum adsorption, also removes color and odor
Cons: High cost, spent carbon disposal/regeneration, saturation limits
Other Adsorbents
- Resins: Targeted organic removal, high cost
- Zeolites: Better for ammonia than COD
- Bentonite/clay: Low cost but low efficiency
- Biochar: Emerging low-cost option, variable quality
5. Membrane Processes
Reverse Osmosis (RO)
- COD removal: 90 – 99%
- Effluent quality: Excellent, suitable for reuse
- Disadvantages: High capital cost, concentrate disposal, membrane fouling
- Best for: Water reuse applications, strict discharge limits
Nanofiltration (NF)
- COD removal: 50 – 90%
- Better for: Color and organic micro-pollutants than total COD
- Lower operating pressure than RO
Choosing the Right COD Removal Method
By Influent COD Concentration
| COD Range | Recommended Primary Method | Secondary Method |
|---|---|---|
| < 200 mg/L | Activated carbon adsorption, AOP polishing | Membrane filtration |
| 200 – 1,000 mg/L | Coagulation + biological | AOP polishing |
| 1,000 – 3,000 mg/L | Biological (aerobic) | Chemical primary + tertiary |
| 3,000 – 10,000 mg/L | Anaerobic + aerobic | Chemical tertiary |
| > 10,000 mg/L | Anaerobic (UASB/IC) | Aerobic + polishing |
By Wastewater Type
| Industry | Typical COD | Recommended Treatment Train |
|---|---|---|
| Municipal sewage | 200 – 500 mg/L | Primary sedimentation + activated sludge + disinfection |
| Textile dyeing | 500 – 3,000 mg/L | Coagulation + biological + Fenton/ozone |
| Pulp & paper | 1,000 – 5,000 mg/L | Primary coagulation + anaerobic + aerobic + tertiary |
| Chemical/pharma | 2,000 – 20,000 mg/L | Anaerobic + aerobic + AOP + activated carbon |
| Food & beverage | 2,000 – 10,000 mg/L | Anaerobic + aerobic (highly biodegradable) |
| Landfill leachate | 5,000 – 30,000 mg/L | Anaerobic + MBR + RO + AOP |
Cost Comparison
| Treatment Method | Capital Cost (USD/m³/day) | Operating Cost (USD/m³) | Sludge Disposal Cost |
|---|---|---|---|
| Coagulation-sedimentation | $50 – $150 | $0.10 – $0.30 | Medium |
| Activated sludge | $100 – $250 | $0.05 – $0.20 | Medium |
| MBR | $200 – $500 | $0.15 – $0.40 | Low |
| UASB anaerobic | $150 – $350 | $0.02 – $0.08 | Very low |
| Fenton oxidation | $80 – $200 | $0.30 – $1.00 | High |
| Ozonation | $200 – $500 | $0.40 – $1.20 | None |
| Activated carbon (GAC) | $50 – $150 | $0.20 – $0.80 | High (spent carbon) |
| RO membrane | $300 – $800 | $0.50 – $1.50 | Concentrate |
Optimization Tips
- Start with jar tests: Always conduct laboratory jar tests before implementing any chemical treatment program
- Maximize biological treatment first: Biological processes are the cheapest way to remove biodegradable COD
- Optimize pH: Both coagulation and AOPs are highly pH-dependent
- Consider combination processes: PAC + PFS coagulation, Fenton + coagulation, biological + AOP
- Reduce at source: Improve production processes to reduce COD load before treatment
- Monitor regularly: Continuous COD monitoring helps optimize dosing and detect process upsets early
Conclusion
Effective COD removal requires matching the right technology to your specific wastewater characteristics. For most industrial applications, a multi-stage approach combining biological treatment with chemical coagulation and/or advanced oxidation produces the best balance of cost and performance. The key is to maximize low-cost biological removal first, then use more expensive chemical methods only for the remaining refractory COD.
Need help designing a COD removal system for your wastewater? Contact our technical team for a free evaluation and treatment recommendation.
Related Resources: