Case Study: Ozone for Industrial Odor Control in Exhaust Gas Treatment — System Design, Performance Data, and Cost Comparison
The Growing Challenge of Industrial Odor Emissions
Industrial facilities across waste treatment, food processing, chemical manufacturing, and pharmaceutical production face increasingly stringent regulations on odor emissions. Complaints from surrounding communities, regulatory fines, and environmental compliance requirements have made odor control a critical operational priority for plant managers worldwide.
Ozone (O₃) has emerged as one of the most powerful oxidizing agents for odor control, capable of destroying odor-causing compounds at the molecular level. Unlike chemical scrubbers that merely transfer pollutants to a liquid waste stream, ozone chemically decomposes malodorous compounds — including hydrogen sulfide (H₂S), mercaptans, volatile organic compounds (VOCs), and amines — into odorless, harmless byproducts such as water, oxygen, and sulfates.
This case study examines a real-world implementation of an ozone-based odor control system at an industrial organic waste processing facility, covering system design, equipment selection, performance data, and a detailed cost comparison with conventional chemical scrubbing technology.
Client Background and Project Requirements
The client operates a mid-sized organic waste processing and composting facility in Southeast Asia, processing approximately 200 tons of organic waste per day. The facility's exhaust gas streams contained complex mixtures of malodorous compounds at elevated concentrations.
The facility had been using a two-stage chemical scrubber system (acid + caustic) but faced three persistent problems:
- High chemical consumption — NaOH and H₂SO₄ costs exceeded $45,000 annually
- Secondary wastewater — spent scrubbing liquid required additional treatment before discharge
- Incomplete odor removal — neighbor complaints continued during peak loading events
The client required a solution that could achieve over 95% odor removal, reduce operating costs, and eliminate secondary wastewater generation entirely.
System Design and Equipment Selection
Ozone Generation Capacity Sizing
The odor control system was designed around two parallel exhaust streams, each handling 5,000 m³/h of exhaust gas. Based on pilot testing and the stoichiometric analysis of target compounds, the ozone demand was calculated and a safety factor applied:
| Parameter | Stream A (Composting Hall) | Stream B (Processing Area) |
|---|---|---|
| Gas flow rate | 5,000 m³/h | 5,000 m³/h |
| H₂S concentration (peak) | 120 ppm | 80 ppm |
| Calculated ozone dose | 25 g/h | 18 g/h |
| With safety factor (1.5×) | 37.5 g/h | 27 g/h |
| Selected generator capacity | 40 g/h | 30 g/h |
Two oxygen-fed, water-cooled ozone generators were selected for maximum ozone concentration and oxidation efficiency. Oxygen-fed systems achieve ozone concentrations of 6–10 wt%, compared to only 2–3 wt% from air-fed units, ensuring faster and more complete odor compound destruction.
Reaction Chamber and Contact Time
Effective odor destruction requires sufficient contact time between ozone and the target compounds. The system incorporated a stainless steel reaction chamber with a designed gas residence time of 8–12 seconds, optimized for the reaction kinetics of H₂S and mercaptan oxidation.
An ozone destruct unit was installed downstream to catalytically decompose residual ozone before atmospheric discharge, ensuring outlet ozone levels remained below 0.1 ppm — well within international occupational safety limits.
Installation and Commissioning
The complete system was installed over a three-week period, including the following major components:
- PSA oxygen concentrator (93% purity, 10 L/min output)
- Two water-cooled ozone generators (40 g/h + 30 g/h)
- Stainless steel reaction chambers with integrated static mixers
- Catalytic ozone destruct unit (manganese dioxide catalyst)
- PLC control system with HMI touchscreen interface
- Ozone gas concentration monitors at inlet and outlet
Commissioning included a two-week optimization phase during which ozone dosage was fine-tuned to match variable odor loads. The PLC system was programmed with a feedback control loop that automatically adjusts ozone output based on real-time H₂S sensor readings, ensuring optimal performance without ozone waste.
Performance Results
After three months of continuous operation, the system consistently achieved the following removal efficiencies across all major odor compounds:
| Odor Compound | Inlet Concentration | Outlet Concentration | Removal Efficiency |
|---|---|---|---|
| Hydrogen sulfide (H₂S) | 50–120 ppm | <2 ppm | >97% |
| Ammonia (NH₃) | 30–80 ppm | 8–15 ppm | >75% |
| Mercaptans | 15–40 ppm | <1 ppm | >95% |
| Total VOCs | 20–50 ppm | 5–12 ppm | >70% |
| Total odor concentration | 8,000–15,000 OU/m³ | 400–800 OU/m³ | >94% |
“After switching to the ozone-based system, we eliminated all neighbor complaints within the first month. The facility now meets local environmental standards with zero chemical consumption and no secondary wastewater to treat.”
— Plant Operations Manager
Cost Comparison: Ozone vs. Chemical Scrubbers
A 24-month total cost of ownership (TCO) analysis compared the ozone system with the previous chemical scrubber setup. The results demonstrate dramatic savings across nearly every cost category:
| Cost Category | Chemical Scrubber (Annual) | Ozone System (Annual) | Savings |
|---|---|---|---|
| Chemicals (NaOH, H₂SO₄) | $45,000 | $0 | $45,000 |
| Electricity | $8,000 | $12,500 | -$4,500 |
| Wastewater treatment | $15,000 | $0 | $15,000 |
| Maintenance & parts | $7,000 | $3,500 | $3,500 |
| Labor | $6,000 | $3,000 | $3,000 |
| Total annual cost | $81,000 | $19,000 | $62,000 |
The ozone system delivered a 76% reduction in annual operating costs, with a payback period of approximately 14 months against the total system investment of $72,000 for equipment and installation.
Key Lessons and Best Practices
Based on this implementation and subsequent projects, several best practices emerge for ozone-based odor control systems:
- Always conduct pilot testing. Odor compound profiles vary significantly between facilities. Pilot data is essential for accurate ozone dose calculation and system sizing.
- Use oxygen-fed generators. Air-fed units produce lower ozone concentrations (2–3 wt%), reducing oxidation efficiency. Oxygen-fed systems achieve 6–10 wt%, ensuring faster and more complete odor destruction.
- Design for variable loads. Industrial odor emissions fluctuate with production cycles. A PLC-based feedback control system with real-time sensors ensures optimal ozone dosage without waste.
- Include an ozone destruct unit. Residual ozone must be catalytically decomposed before atmospheric release to ensure compliance with environmental and occupational safety standards.
- Size for peak, not average. Undersized systems fail during peak loading events. Apply a safety factor of at least 1.5× to the calculated ozone demand.
Conclusion
This case study demonstrates that ozone-based odor control systems can deliver superior performance compared to conventional chemical scrubbers while dramatically reducing operating costs and eliminating secondary pollution. With over 94% total odor removal, 76% annual cost savings, and a 14-month payback period, ozone technology offers industrial facilities a compelling combination of effectiveness, economy, and environmental compliance for exhaust gas odor treatment.
Contact Tonglin Ozone for professional ozone solutions.
Email: l810185168@gmail.com
Phone/WhatsApp: 15818868390
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