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Said Abou Abdallah, Terry Keep and Dr. Dean Reynolds
Ohio AWWA
September 20, 2012
The City of Alliance's Solution for
Taste and Odor Treatment
2
WATER STRESS
IN AN
INTERCONNECTED
WATER SUPPLY
Sources of contaminants in
our water supply:
- Industrial discharge
- Agricultural runoff
- Chemical releases
- Municipal Wastewater
Injection
Well
Extraction
Well
Nutrients  increase in Algae Blooms  Taste & Odour, Algal Toxins
3
EXAMPLES OF MICROPOLLUTANTS
Nitrosamines (e.g. NDMA)
Disinfection byproducts
Pesticides & Herbicides
Metaldehyde, Atrazine, Isoproturon, others
Petroleum Additives
Including MTBE
Pharmaceuticals & Personal Care Products
Includes potential endocrine disruptors
Taste & Odour Compounds
Seasonal occurrences of MIB, geosmin and others
Algal Toxins
Chronic and acute effects from cyanobacteria-derived
toxins
4
TASTE & ODOUR, ALGAL TOXINS
Seasonal algae blooms occur in surface
waters
Decaying algae blooms result in MIB,
geosmin, algal toxins, other T&O
compounds
Earthy/musty, fishy, swampy, grassy
tastes & odours at low ppt
concentrations
Difficult to remove with conventional
technologies
T&O episodes compromise public
confidence in the safety of the water
5
COMPOUNDS GENERATED BY SOME CYANOBACTERIA
Geosmin
2-Methylisoborneol (MIB)
GSMand MIBcan be detected
by sensitive individual down to
4 ng/L (ppt)
[Geosmin] have been
measured > 3000 ng/L
Aesthetics: T&O cmpds
Cylindrospermopsin (CYN)
Microcystin-LR (MC-LR) [MC]~1800ug/L meas drng bloom
Public Health: Cyanotoxins
W
HO
set lim
it at 1
µg/L
USEPA
added
CNTX
to
the
CCL
6
TASTE AND ODOUR TREATMENT STRATEGIES
• Potassium Permanganate
– Limited Effectiveness
• Powdered Activated Carbon
– Messy PAC & Sludge Handling, no Performance Guarantee
• Granular Activated Carbon
– Frequent & Expensive Change-outs, no Performance Guarantee
• Ozone
– Complicated System & Carcinogenic by-product (Bromate)
• UV-Oxidation
– Simple, Effective for T&O with Simultaneous Disinfection, Guaranteed
Performance for life of system
7
UV / H2O2 FOR TASTE AND ODOUR TREATMENT
UV Advanced Oxidation: Using UV and Hydrogen Peroxide to destroy
trace organic contaminants in water by:
UV-Photolysis
UV-Oxidation
8
UV-PHOTOLYSIS
Chemical bonds are
broken by UV light
9
UV-OXIDATION
Hydrogen
peroxide
Hydroxyl
radical
Chemical bonds are
broken by hydroxyl
radicals
Planning and Engineering
Approach to the Final Design
11
Planning and Engineering Approach to the
Final Design
o UV Oxidation System Feasibility Study
o UV Oxidation System Procurement
o UV Oxidation System Final Design Documents
o Design Criteria:
• UVT 92%
• Turbidity < 0.06 NTU
• TOC < 3 mg/l
• Nitrates < 1 mg/l
• pH 6.7 – 6.9
• Average Flow 5.5 MGD/10.0 MGD Max
12
UV Oxidation System Feasibility Study
• Actual Costs of using Powered
Activated Carbon (PAC)
• UV Oxidation Process
• Electrical Costs
• Hydrogen Peroxide Cost
• Chlorination Cost
• Equipment Manufacturer's Variations
• Design Requirements
• Non-Cost factors
13
UV Oxidation System Feasibility Study
• PAC (Powder Activated Carbon)
System Capabilities and
Limitations
• Type of PAC used
• Impact on Other Treatment
Processes
• Operational Difficulties
• Future Limitations
14
Actual PAC CostsMonth
Days/
Month
Average Influent
MIB Concentration
Flow PAC Cost / MG / day PAC Cost
June, 2010 30 125.53 3.2 $27.76 $2,665.23
July, 2010 31 86.50 3.7 $14.82 $1,700.29
August, 2010 31 23.07 3.5 $17.50 $1,899.18
September, 2010 30 25.90 3.4 $14.89 $1,519.20
October, 2010 31 112.33 3.2 $131.74 $13,068.90
November, 2010 30 326.63 3.0 $422.42 $38,017.41
December, 2010 31 549.46 3.2 $559.86 $55,538.10
January, 2011 31 967.06 3.3 $521.49 $53,348.20
February, 2011 28 911.53 3.3 $535.70 $49,498.78
March, 2011 31 125.67 3.2 $513.44 $50,933.69
April, 2011 30 11.05 3.2 $72.31 $6,941.88
May, 2011 31 4.65 3.7 $22.18 $2,544.50
12 Months Total $277,675.37
Actual Costs of PAC Treatment
15
PAC Actual vs. UV Ox ProjectionsMonth and Year
Average Influent
MIB Concentration
Average Flow
(MGD)
Actual PAC Costs
Projected PAC/
UV Ox Costs
June, 2010 125.53 3.2 $2,665.23 $2,665.23
July, 2010 86.50 3.7 $1,700.29 $1,700.29
August, 2010 23.07 3.5 $1,899.18 $1,899.18
September, 2010 25.90 3.4 $1,519.20 $1,519.20
October, 2010 112.33 3.2 $13,068.90 $13,068.90
November, 2010 326.63 3.0 $38,017.41 $27,000.00
December, 2010 549.46 3.2 $55,538.10 $48,087.57
January, 2011 967.06 3.3 $53,348.20 $57,364.10
February, 2011 911.53 3.3 $49,498.78 $52,469.39
March, 2011 125.67 3.2 $50,933.69 $29,760.00
April, 2011 11.05 3.2 $6,941.88 $6,941.88
May, 2011 4.65 3.7 $2,544.50 $2,544.50
12 Months Total $277,675.37 $245,020.24
PAC Actual vs. UV Ox Projected
16
MIB Concentration vs. PAC and UV Ox
17
UV Oxidation System Feasibility Study:
Findings
• Procurement Recommendations for UV Oxidation System
• Capital Costs and Operation & Maintenance Costs
• Non-Cost Factors (Vendor Experience)
• Impact on Water Users – Water rate, water quality
• Schedule of Implementation
18
UV Oxidation System Procurement
• Traditional Design vs. Pre-selection
• Variations with Manufacturer’s
Designs
• UV Oxidation Equipment Essential
and Critical for Taste and Odor
• UV Oxidation Equipment Represents
Significant Project Cost
• Multiple Available Strategies
• Balancing Qualifications/Experience
and Costs
• Early Procurement Prevents
Duplications and Delays
19
UV Oxidation System
Procurement:
Key Considerations
• Tight Procurement
Documents
• Scope of Equipment
• Warranty
• Proposal Information
• Operating Parameters
• Capital Cost Analysis vs.
Present Worth Analysis
• Bidding Conditions
• Decision Analysis and
Weighting
20
UV Oxidation System: Procurement
• Bid items
• Clear and specific
• Bid Requirements
• Financial Stability
• Experience and Past Performance
• Demonstration of successful
Operations
• Equipment Service and
Support
• Equipment Characteristics and
Flexibility
• Future Capacity
• Operations and Complexity
21
UV Oxidation System: Procurement
• Cost Factors:
• Capital Cost
• O&M Cost
• Common Cost Parameters
• Energy Cost
• Chemical Cost
• Interest rates
• PW period
22
UV Oxidation System:
Effective Integration of Quality and Cost
• Designed to meet the
Client and Project Goals
• Balanced between Cost
and Non-Cost Factors
• Qualifications/Experience
Emphasis
• Broad Spectrum of
Evaluation
23
UV Oxidation System:
Final Design Documents
• Design Documents to Allow the Installation of
the Procured Equipment
• UV Oxidation Units
• Hydrogen Peroxide Feed and Storage System
• Chlorine Feed System
• Future Provisions
• Performance Testing
24
UV Oxidation System:
Final Design Documents
• Two 30-Inch Diameter Reactor in Series
• Cooling System for Use During Filter
Backwash Operations
• Operator Input During Chlorine Trouble Times
• Dedicated Automatic Chlorinator for UV Ox Operation
• System Bypass During Non- Taste and Odor Season
25
UV Oxidation System:
Final Design Documents
• Hydrogen Peroxide System
• One 3,000 Gallon Hydrogen Peroxide Bulk
Storage Tank
• Two Day tanks with Duplex Feed pump
System
• Double Containment Piping
• Chlorine Feed System Capacity Upgrade
• New Chlorine Evaporator
• Dedicated Chlorinator for UV Ox
• Use of Liquid Chlorine with Back-up Gas
Manifolds
• Re-training of personnel on use of new
Chlorine System
26
UV Oxidation System:
Final Design Documents
• Future Chloramination
• Provisions for Feed System
• Provisions for Multiple
Monitoring Locations
• Implementation Schedule
• Construction Project Bidding
in September/October 2012
• Construction NTP November 2012
• Substantial Completion September 20132013
• Performance Testing by December 2013
SWIFT ECT 16L30” UV Reactor
30” Reactor
On line UV
Transmittance
Monitor
28
QUESTIONS?
Terry Keep
ECT Sales Manager
Trojan Technologies
519.457.3400
tkeep@trojanuv.com
Said AbouAbdallah, PE | Associate Vice President
Malcolm Pirnie | The Water Division of ARCADIS
216.781.6177
said.abouabdallah @arcadis-us.com

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Ohio AWWA City of Alliance Selection of UV Oxidation for Taste & Odor treatment

  • 1. Said Abou Abdallah, Terry Keep and Dr. Dean Reynolds Ohio AWWA September 20, 2012 The City of Alliance's Solution for Taste and Odor Treatment
  • 2. 2 WATER STRESS IN AN INTERCONNECTED WATER SUPPLY Sources of contaminants in our water supply: - Industrial discharge - Agricultural runoff - Chemical releases - Municipal Wastewater Injection Well Extraction Well Nutrients  increase in Algae Blooms  Taste & Odour, Algal Toxins
  • 3. 3 EXAMPLES OF MICROPOLLUTANTS Nitrosamines (e.g. NDMA) Disinfection byproducts Pesticides & Herbicides Metaldehyde, Atrazine, Isoproturon, others Petroleum Additives Including MTBE Pharmaceuticals & Personal Care Products Includes potential endocrine disruptors Taste & Odour Compounds Seasonal occurrences of MIB, geosmin and others Algal Toxins Chronic and acute effects from cyanobacteria-derived toxins
  • 4. 4 TASTE & ODOUR, ALGAL TOXINS Seasonal algae blooms occur in surface waters Decaying algae blooms result in MIB, geosmin, algal toxins, other T&O compounds Earthy/musty, fishy, swampy, grassy tastes & odours at low ppt concentrations Difficult to remove with conventional technologies T&O episodes compromise public confidence in the safety of the water
  • 5. 5 COMPOUNDS GENERATED BY SOME CYANOBACTERIA Geosmin 2-Methylisoborneol (MIB) GSMand MIBcan be detected by sensitive individual down to 4 ng/L (ppt) [Geosmin] have been measured > 3000 ng/L Aesthetics: T&O cmpds Cylindrospermopsin (CYN) Microcystin-LR (MC-LR) [MC]~1800ug/L meas drng bloom Public Health: Cyanotoxins W HO set lim it at 1 µg/L USEPA added CNTX to the CCL
  • 6. 6 TASTE AND ODOUR TREATMENT STRATEGIES • Potassium Permanganate – Limited Effectiveness • Powdered Activated Carbon – Messy PAC & Sludge Handling, no Performance Guarantee • Granular Activated Carbon – Frequent & Expensive Change-outs, no Performance Guarantee • Ozone – Complicated System & Carcinogenic by-product (Bromate) • UV-Oxidation – Simple, Effective for T&O with Simultaneous Disinfection, Guaranteed Performance for life of system
  • 7. 7 UV / H2O2 FOR TASTE AND ODOUR TREATMENT UV Advanced Oxidation: Using UV and Hydrogen Peroxide to destroy trace organic contaminants in water by: UV-Photolysis UV-Oxidation
  • 10. Planning and Engineering Approach to the Final Design
  • 11. 11 Planning and Engineering Approach to the Final Design o UV Oxidation System Feasibility Study o UV Oxidation System Procurement o UV Oxidation System Final Design Documents o Design Criteria: • UVT 92% • Turbidity < 0.06 NTU • TOC < 3 mg/l • Nitrates < 1 mg/l • pH 6.7 – 6.9 • Average Flow 5.5 MGD/10.0 MGD Max
  • 12. 12 UV Oxidation System Feasibility Study • Actual Costs of using Powered Activated Carbon (PAC) • UV Oxidation Process • Electrical Costs • Hydrogen Peroxide Cost • Chlorination Cost • Equipment Manufacturer's Variations • Design Requirements • Non-Cost factors
  • 13. 13 UV Oxidation System Feasibility Study • PAC (Powder Activated Carbon) System Capabilities and Limitations • Type of PAC used • Impact on Other Treatment Processes • Operational Difficulties • Future Limitations
  • 14. 14 Actual PAC CostsMonth Days/ Month Average Influent MIB Concentration Flow PAC Cost / MG / day PAC Cost June, 2010 30 125.53 3.2 $27.76 $2,665.23 July, 2010 31 86.50 3.7 $14.82 $1,700.29 August, 2010 31 23.07 3.5 $17.50 $1,899.18 September, 2010 30 25.90 3.4 $14.89 $1,519.20 October, 2010 31 112.33 3.2 $131.74 $13,068.90 November, 2010 30 326.63 3.0 $422.42 $38,017.41 December, 2010 31 549.46 3.2 $559.86 $55,538.10 January, 2011 31 967.06 3.3 $521.49 $53,348.20 February, 2011 28 911.53 3.3 $535.70 $49,498.78 March, 2011 31 125.67 3.2 $513.44 $50,933.69 April, 2011 30 11.05 3.2 $72.31 $6,941.88 May, 2011 31 4.65 3.7 $22.18 $2,544.50 12 Months Total $277,675.37 Actual Costs of PAC Treatment
  • 15. 15 PAC Actual vs. UV Ox ProjectionsMonth and Year Average Influent MIB Concentration Average Flow (MGD) Actual PAC Costs Projected PAC/ UV Ox Costs June, 2010 125.53 3.2 $2,665.23 $2,665.23 July, 2010 86.50 3.7 $1,700.29 $1,700.29 August, 2010 23.07 3.5 $1,899.18 $1,899.18 September, 2010 25.90 3.4 $1,519.20 $1,519.20 October, 2010 112.33 3.2 $13,068.90 $13,068.90 November, 2010 326.63 3.0 $38,017.41 $27,000.00 December, 2010 549.46 3.2 $55,538.10 $48,087.57 January, 2011 967.06 3.3 $53,348.20 $57,364.10 February, 2011 911.53 3.3 $49,498.78 $52,469.39 March, 2011 125.67 3.2 $50,933.69 $29,760.00 April, 2011 11.05 3.2 $6,941.88 $6,941.88 May, 2011 4.65 3.7 $2,544.50 $2,544.50 12 Months Total $277,675.37 $245,020.24 PAC Actual vs. UV Ox Projected
  • 16. 16 MIB Concentration vs. PAC and UV Ox
  • 17. 17 UV Oxidation System Feasibility Study: Findings • Procurement Recommendations for UV Oxidation System • Capital Costs and Operation & Maintenance Costs • Non-Cost Factors (Vendor Experience) • Impact on Water Users – Water rate, water quality • Schedule of Implementation
  • 18. 18 UV Oxidation System Procurement • Traditional Design vs. Pre-selection • Variations with Manufacturer’s Designs • UV Oxidation Equipment Essential and Critical for Taste and Odor • UV Oxidation Equipment Represents Significant Project Cost • Multiple Available Strategies • Balancing Qualifications/Experience and Costs • Early Procurement Prevents Duplications and Delays
  • 19. 19 UV Oxidation System Procurement: Key Considerations • Tight Procurement Documents • Scope of Equipment • Warranty • Proposal Information • Operating Parameters • Capital Cost Analysis vs. Present Worth Analysis • Bidding Conditions • Decision Analysis and Weighting
  • 20. 20 UV Oxidation System: Procurement • Bid items • Clear and specific • Bid Requirements • Financial Stability • Experience and Past Performance • Demonstration of successful Operations • Equipment Service and Support • Equipment Characteristics and Flexibility • Future Capacity • Operations and Complexity
  • 21. 21 UV Oxidation System: Procurement • Cost Factors: • Capital Cost • O&M Cost • Common Cost Parameters • Energy Cost • Chemical Cost • Interest rates • PW period
  • 22. 22 UV Oxidation System: Effective Integration of Quality and Cost • Designed to meet the Client and Project Goals • Balanced between Cost and Non-Cost Factors • Qualifications/Experience Emphasis • Broad Spectrum of Evaluation
  • 23. 23 UV Oxidation System: Final Design Documents • Design Documents to Allow the Installation of the Procured Equipment • UV Oxidation Units • Hydrogen Peroxide Feed and Storage System • Chlorine Feed System • Future Provisions • Performance Testing
  • 24. 24 UV Oxidation System: Final Design Documents • Two 30-Inch Diameter Reactor in Series • Cooling System for Use During Filter Backwash Operations • Operator Input During Chlorine Trouble Times • Dedicated Automatic Chlorinator for UV Ox Operation • System Bypass During Non- Taste and Odor Season
  • 25. 25 UV Oxidation System: Final Design Documents • Hydrogen Peroxide System • One 3,000 Gallon Hydrogen Peroxide Bulk Storage Tank • Two Day tanks with Duplex Feed pump System • Double Containment Piping • Chlorine Feed System Capacity Upgrade • New Chlorine Evaporator • Dedicated Chlorinator for UV Ox • Use of Liquid Chlorine with Back-up Gas Manifolds • Re-training of personnel on use of new Chlorine System
  • 26. 26 UV Oxidation System: Final Design Documents • Future Chloramination • Provisions for Feed System • Provisions for Multiple Monitoring Locations • Implementation Schedule • Construction Project Bidding in September/October 2012 • Construction NTP November 2012 • Substantial Completion September 20132013 • Performance Testing by December 2013
  • 27. SWIFT ECT 16L30” UV Reactor 30” Reactor On line UV Transmittance Monitor
  • 28. 28 QUESTIONS? Terry Keep ECT Sales Manager Trojan Technologies 519.457.3400 tkeep@trojanuv.com Said AbouAbdallah, PE | Associate Vice President Malcolm Pirnie | The Water Division of ARCADIS 216.781.6177 said.abouabdallah @arcadis-us.com

Editor's Notes

  1. May 6, 2013
  2. May 6, 2013
  3. May 6, 2013
  4. May 6, 2013
  5. Start here with Gary’s dwgs May 6, 2013