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About This Playbook: This guide provides systematic approaches to identifying, diagnosing, and resolving odour issues in wastewater treatment facilities. It is designed for operators managing industrial and municipal WWTPs across Australia and New Zealand.
1. Understanding Odour Sources
Primary Odour Compounds
Compound
Source
Characteristics
Threshold (ppm)
H₂S (Hydrogen Sulphide)
Anaerobic decomposition of sulphur-containing proteins
Rotten egg smell, highly toxic
0.0005
NH₃ (Ammonia)
Protein breakdown, urea decomposition
Pungent, irritating
5.0
Mercaptans
FOG decomposition, industrial waste
Skunk-like, cabbage
0.001
VFAs (Volatile Fatty Acids)
Incomplete anaerobic digestion
Sour, vinegar-like
0.001-1.0
Indoles/Skatoles
Protein fermentation
Fecal odour
0.001
Common Odour Generation Points
Influent Collection Systems: Long retention times, anaerobic conditions in sewers
Primary Treatment: Screens, grit chambers, primary clarifiers
Aeration Basins: Under-aerated zones, dead spots, surfacing sludge
Secondary Clarifiers: Septic sludge, poor sludge blanket management
Sludge Handling: Thickening, digestion, dewatering operations
Lagoons: Turnover events, stratification, anaerobic bottom layers
2. Diagnostic Protocol
Systematic Odour Investigation
1
Initial Assessment
When does odour occur? (time of day, weather conditions)
Where is it most intense? (specific units, areas)
Character of odour? (rotten egg, septic, chemical)
Community complaints? (frequency, severity)
2
Field Measurements
Dissolved Oxygen (DO) levels at multiple points
H₂S concentration (portable monitor)
pH and temperature profiles
ORP (Oxidation-Reduction Potential) readings
3
Process Review
Sludge age and wasting rates
Hydraulic retention time (HRT)
F/M ratio and organic loading
Return activated sludge (RAS) rates
4
Root Cause Analysis
Compare findings against normal operating ranges
Identify process deviations
Determine primary vs. secondary causes
Develop corrective action plan
3. Common Problems & Solutions
Problem: H₂S Generation in Clarifiers
Symptoms: Rotten egg smell, black discoloration of sludge, corrosion of concrete surfaces
Root Causes:
Excessive sludge blanket depth (>1.5m)
Low DO in return activated sludge (<0.5 mg/L)
Long sludge retention in clarifier (>2 hours)
High sulfate-containing industrial discharge
Solutions:
Immediate: Increase RAS rate to reduce sludge blanket, increase DO in aeration basin
Short-term: Apply bioaugmentation products to oxidize sulfides, add nitrate to clarifier
Long-term: Optimize sludge wasting schedule, implement DO setpoint control, work with industries on sulfate reduction
Problem: Lagoon Turnover Events
Symptoms: Sudden, severe odour release; dark water color; fish kills; gas bubbling
Root Causes:
Thermal stratification breakdown (seasonal temperature change)
Heavy rainfall causing rapid mixing
Deep anaerobic sludge layer accumulation
Wind-driven destratification
Solutions:
Prevention: Regular mechanical mixing/aeration, seasonal sludge surveys, controlled turnover scheduling
During Event: Maximize aeration, apply hydrogen peroxide or nitrate, deploy floating aerators
Recovery: Bioaugmentation to re-establish aerobic microbial community, monitor DO continuously for 2 weeks
Problem: Abattoir Wastewater Odours
Symptoms: Intense putrefaction odours, FOG accumulation, rapid pH drops, white/grey foam
Root Causes:
High protein and FOG loads overwhelming treatment
Anaerobic zones created by poor mixing
Temperature spikes from hot wash-down water
Inadequate nutrient balance (N:P deficiency)
Solutions:
Source Control: Install better FOG removal (dissolved air flotation), cool influent before treatment
Process Optimisation: Increase aeration capacity, add nutrients (urea, phosphoric acid)
Bioaugmentation: Apply specialised protein and FOG-degrading cultures, maintain stable microbial population
Monitoring: Daily protein testing, weekly microscopy to assess microbial health
4. Bioaugmentation Protocols
When to Use Bioaugmentation
Persistent odour issues despite process optimisation
After toxic shock or plant upset
High-strength industrial waste events
Startup or restart situations
Seasonal loading changes
Application Guidelines
Parameter
Requirement
Notes
DO Level
>1.0 mg/L
Essential for aerobic culture survival
pH Range
6.5 - 8.5
Optimize to 7.0 - 7.5 for best results
Temperature
15 - 35°C
Activity doubles every 10°C rise
Mixing
Continuous
Prevent settling, ensure contact
Contact Time
>4 hours HRT
Longer is better for establishment
Expected Timeline:
Week 1-2: Culture acclimatization, initial colonization
Week 2-4: Measurable H₂S reduction (typically 40-60%)
Week 4-8: Full odour control establishment (70-90% reduction)
Ongoing: Maintenance dosing as needed
5. Operator Checklist
Daily Monitoring
Visual inspection of all treatment units
DO readings at aeration basin inlet, middle, and outlet
Sludge blanket level in clarifiers
Note any unusual odours (location, intensity, character)
Check foam levels and color
Review weather conditions and temperature
Weekly Assessment
BOD/COD testing of influent and effluent
Suspended solids analysis
Microscopic examination of mixed liquor
Sludge volume index (SVI) testing
Review community complaint log
Check chemical inventory and dosing equipment
Monthly Review
Comprehensive process performance analysis
Trend analysis of key parameters
Equipment maintenance verification
Lagoon bathymetry (if applicable)
Bioaugmentation effectiveness assessment
Update odour management plan as needed
6. Emergency Response
Acute Odour Event Protocol
Immediate: Notify supervisor, document time and location, check H₂S levels for safety
First Hour: Maximize aeration, inspect for obvious causes (spills, equipment failure), notify neighbors if severe
First 4 Hours: Implement emergency treatment (H₂O₂, nitrate, or iron salts), collect samples for lab analysis
First 24 Hours: Apply bioaugmentation products, develop corrective action plan, prepare incident report
Follow-up: Daily monitoring until resolved, review prevention measures
Safety Considerations
H₂S Safety Thresholds:
10 ppm: OSHA 8-hour exposure limit
15 ppm: Short-term exposure limit (15 min)
100 ppm: IDLH (Immediately Dangerous to Life or Health)
>500 ppm: Fatal after 30 minutes
Always: Use personal H₂S monitors, work in pairs, ensure proper ventilation, have emergency evacuation plan
7. Key Performance Indicators
Parameter
Target Range
Action Required If Outside Range
Aeration Basin DO
2.0 - 4.0 mg/L
Adjust blower output, check diffusers
RAS DO
>0.5 mg/L
Increase aeration, reduce RAS rate temporarily
H₂S (headspace)
<5 ppm
Investigate source, implement bioaugmentation
pH
6.8 - 7.5
Adjust with lime or acid, investigate cause
ORP
>0 mV (aerobic zones)
Increase aeration, check for anaerobic pockets
Sludge Blanket
<1.0 m
Increase RAS, optimise wasting
F/M Ratio
0.2 - 0.5 kg BOD/kg MLSS/day
Adjust wasting rate or influent flow
8. Resources & Contacts
Recommended Testing Schedule
Critical Parameters (Daily): DO, pH, temperature, visual inspection
Process Control (Weekly): BOD/COD, TSS, MLSS, SVI, microscopy
Comprehensive (Monthly): Nutrients, metals, full suite analysis
Technical Support
Bio Solve Solutions
Phone: +64 27 240 4195
Email: louis@lohill.co.nz
Website: www.biosolvesolutions.com
Emergency Support: Available 24/7 for critical odour events
Pilot Programs: Free 30-day trials available for bioaugmentation solutions
Additional Resources
Water Environment Federation (WEF) Manual of Practice No. 25: Odor Control
Australian Water Association (AWA) technical papers
WWTP Operator Certification programs
Micro-Genix online knowledge base and video tutorials
9. Case Studies
Case Study 1: Municipal WWTP - Clarifier H₂S Control
Facility: 5 ML/day municipal plant, oxidation ditch + clarifiers
Problem: Persistent H₂S odours from secondary clarifiers, complaints from nearby residential area
Root Cause: Excessive sludge blanket (2.3m avg), low RAS DO (0.2 mg/L), long clarifier retention (>3 hrs)
Solution Implemented:
Increased RAS rate from 60% to 85% of influent flow
Applied sulfide-oxidizing bioaugmentation product
Optimized DO setpoint to 2.5 mg/L in oxidation ditch
Results:
H₂S reduced from 45 ppm to 3 ppm within 3 weeks
Zero odour complaints after 4 weeks
Maintained control with maintenance dosing (2x/week)
Case Study 2: Red Meat Processing - FOG & Protein Odours
Facility: Abattoir with 800 m³/day high-strength waste, DAF + lagoon system
Problem: Intense putrefaction odours, frequent foam events, regulatory complaints
Root Cause: BOD spikes (3,000-8,000 mg/L), FOG overloading (>500 mg/L), insufficient biological activity
Solution Implemented:
Improved FOG removal efficiency in DAF (recovery from 75% to 92%)
Applied specialised protein/lipid-degrading culture
Added supplemental aeration in lagoon cells 1-2
Established nutrient addition protocol (N:P balance)
Results:
Odour intensity reduced by 85% within 6 weeks
Foam events eliminated
BOD removal efficiency improved from 65% to 88%
Regulatory compliance achieved and maintained
10. Troubleshooting Quick Reference
Odour Character
Likely Cause
First Action
Rotten eggs
H₂S from anaerobic conditions
Increase aeration, check DO levels
Ammonia/urine
Protein breakdown, pH issues
Check pH, improve nitrification
Musty/earthy
Actinomycetes overgrowth
Review sludge age, consider wasting
Septic/sewage
Long HRT, insufficient treatment
Increase flow-through, add aeration
Chemical/solvent
Industrial discharge
Trace source, implement pretreatment
Rancid fat
FOG decomposition
Improve grease removal, bioaugmentation