Treatment of 1,4-Dioxane and VOCs for Potable Water Applications - - PowerPoint PPT Presentation

treatment of 1 4 dioxane and vocs
SMART_READER_LITE
LIVE PREVIEW

Treatment of 1,4-Dioxane and VOCs for Potable Water Applications - - PowerPoint PPT Presentation

Advanced Oxidation Processes: Treatment of 1,4-Dioxane and VOCs for Potable Water Applications H2M architects + engineers Sujata Pal-Frank, Project Engineer John R. Collins, P.E. Senior Project Engineer Outline Project Background


slide-1
SLIDE 1

Advanced Oxidation Processes: Treatment of 1,4-Dioxane and VOCs for Potable Water Applications

H2M architects + engineers Sujata Pal-Frank, Project Engineer John R. Collins, P.E. Senior Project Engineer

slide-2
SLIDE 2

Outline

  • Project Background
  • 1,4-Dioxane
  • Advanced Oxidation Processes (AOPs)
  • Water Quality Considerations
  • Pilot Study & Results
slide-3
SLIDE 3

Project Background

  • Potable water supply well
  • Water Quality:
  • Wellhead Treatments Considered:
  • AST
  • GAC
  • AOP

13 water suppliers Max: 33 mg/L 3 water suppliers Max: 4.4 mg/L Tetrachloroethylene 1,1,1 Trichloroethane 1,4-Dioxane Trichloroethylene 1,1-Dichloroethane cis 1,2-Dichloroethylene Freon 10 & 12

slide-4
SLIDE 4

1,4-Dioxane

  • Stabilizer for chlorinated solvents
  • Wastewater discharge, spills, leaks
  • Common household products
  • 2,000 ug/l to 300,000 ug/l
  • Manufactured Food Additives
  • Probable Human Carcinogen (Group B2)
  • Persistent in the environment
  • Highly soluble
slide-5
SLIDE 5

1,4-Dioxane Regulations

  • EPA Contaminant Candidate List (CCL3)
  • Indicates potential for regulation under SDWA
  • EPA IRIS: 0.35 mg/l in drinking water
  • NYS UOC MCL: 50 mg/L
  • UCMR3: 70% of NYSMCL on Long Island
slide-6
SLIDE 6

Treatment Options Considered

  • Air Stripping
  • Low volatility in water
  • Granular Activated Carbon
  • Hydrophilic
  • Advanced Oxidation Processes (AOPs)
slide-7
SLIDE 7

Advanced Oxidation Processes

Removal of organic materials from water by oxidation using hydroxyl radicals

  • Characteristics
  • Strong oxidant
  • Highly reactive
  • Production Methods:
  • Ozone + Hydrogen

Peroxide

  • UV + Titanium Dioxide
  • UV + Hydrogen Peroxide
  • UV + Chlorine

Oxidation Species Oxidation Power [V] Fluorine 3.03 Hydroxyl Radical 2.80 Atomic Oxygen 2.42 Positively charged TiO2 2.35 Ozone 2.07 Hydrogen Peroxide 1.77 Permanganate 1.67 Hypochlorous Acid 1.49 Chlorine 1.36 Iodine 0.54

slide-8
SLIDE 8

Advanced Oxidation Processes

Three Steps

  • 1. Form Oxidant
  • 2. Attack target compound
  • 3. Mineralization
slide-9
SLIDE 9

Oxidation

slide-10
SLIDE 10

Oxidation

slide-11
SLIDE 11

Water Quality Considerations

  • pH & Photolysis
  • Hypochlorous Acid v Hypochlorite Ions

HOCI & OCI- OCI - HOCI

slide-12
SLIDE 12

Water Quality Considerations

  • pH & Alkalinity - Scavengers
  • Carbonates (CO3

2- )

pH > 9

  • Bicarbonates (CO3
  • )

pH 7-8

  • Carbonic Acid (H2CO3) pH < 6
  • TOC – Scavengers
  • Nitrate & Nitrite - Scavengers
  • Turbidity & TSS – UV Transmittance (%UVT)
slide-13
SLIDE 13

Pilot Study

  • Partner: Calgon Carbon Corporation
  • Study: UV Oxidation with Chlorine (Calcium

Hypochlorite) to confirm removal efficiency of:

  • 1,4 Dioxane & VOCs
  • Estimated requirements for full scale system
slide-14
SLIDE 14

Sample Raw Water Quality

  • pH
  • Slightly elevated for complete hypochlorous acid

(6.11 vs 5)

  • Slightly elevated alkalinity (Total Alkalinity: 6 to 7 vs <6)
  • TOC : Less than 1 mg/l
  • Nitrate & Nitrite: Nitrite <0.25 mg/l, typical
  • Turbidity & TSS: Low as indicated by high UVT
slide-15
SLIDE 15

Pilot Unit – Batch Design Test

  • Pilot Unit:
  • 1 kW high intensity MP

mercury vapor lamp

  • MP lamps give more light in

200 nm – 260 nm

  • 10 gallon cylindrical

stainless steel reactor

  • Air actuated transmittance

controller (quartz cleaner)

  • Mixer - Chlorine
  • Steel shutter – UV Dosage
slide-16
SLIDE 16

Pilot Procedure

  • 1. Add 30 liters of water sample to unit
  • 2. Ignite UV lamp with shutter closed
  • 3. Dose water with chlorine and mix
  • 4. Open shutter for fixed period of time (UV Dose)
  • 5. Close shutter, take sample, increase UV Dose
  • 6. Repeat steps 4 and 5
  • When residual chlorine measured <0.5, ppm additional

chlorine was added for a target ~1 ppm residual

slide-17
SLIDE 17

Test Results – Run 1

Sample No. UV Dose (kWh/1,000 gal) pH Chlorine (ppm) 1,4-Dioxane (ppb) Raw 0.00 5.82 0.00 37.0 1-0 0.00 6.19 3.80 37.0 1-1 0.60 6.62 2.66 11.0 1-2 1.19 6.12 1.82 2.40 1-3 2.38 6.09 0.60 0.12 1-4 4.76 6.18 0.00 <0.07 Chlorine 1.35 1-5 9.52 6.43 0.00 <0.07

slide-18
SLIDE 18

Test Results – Run 2

Sample No. UV Dose (kWh/1,000 gal) pH Chlorine (ppm) 1,4-Dioxane (ppb) Raw 0.00 5.77 0.00 38.0 1-0 0.00 6.33 6.75 36.0 1-1 0.60 6.24 5.25 13.0 1-2 1.19 6.26 3.60 3.80 1-3 1.90 6.24 2.40 1.00 1-4 3.93 6.22 0.34 <0.07 Chlorine 1.90 1-5 7.14 6.32 0.00 <0.07

slide-19
SLIDE 19

Test Results 1,4-Dioxane

Test Run pH Initial Chlorine Concentration [ppm] Max UV Dose (kWh/1,000gal) 1 6.11 3.80 9.52 2 6.11 6.75 7.14

slide-20
SLIDE 20

Test Results

Compound 1-0 ppb 1-5 ppb 2-0 ppb 2-5 ppb 1,1-DCE 8.36 <0.50 7.78 <0.50 Cis 1,2-DCE 8.13 <0.50 7.84 <0.50 PCE 3.21 <0.50 3.00 <0.50 TCE 11.7 <0.50 11.3 <0.50 Benzene 0.69 <0.50 0.69 <0.50 1,1,1-TCA 2.07 0.54 2.1 0.77 1,1-DCA 17.9 3.78 17.5 5.29 Carbon Tetrachloride 1.69 <0.50 1.59 0.56 Bromodichloromethane <0.50 <0.50 <0.50 0.72 Chloroform <0.50 <0.50 <0.50 0.55

slide-21
SLIDE 21

Test Results

Organic Molecule Rate Constant [mol/L-sec] Chlorinated alkenes 109 to 1011 Phenols 109 to 1010 N-containing organics 108 to 1010 Aromatics 108 to 1010 Ketones 109 to 1010 Alcohols 108 to 109 Alkanes 106 to 109

slide-22
SLIDE 22

Full Scale Operation

  • 1,400 GPM @ 2,200 hrs
  • Two Calgon SentinelTM Reactors
  • Nine 10 kW lamps
slide-23
SLIDE 23

Capital Cost Considerations

  • Process Treatment
  • Well Rehabilitation
  • AOP Reactor - $200,000/reactor
  • Chlorine Bulk Storage System - $80,000
  • AST
  • GAC
  • Buildings/Structure
  • Electrical
  • MCC, Telemetry, Security
  • Primary Service
  • Site Work
slide-24
SLIDE 24

O&M Cost Considerations

  • Electrical Loads
  • Building & Heating Demands (3 systems)
  • GAC Replacement Costs
  • Monitoring & Laboratory Costs
  • Chemical Costs
  • Chlorine – Oxidation
  • Chlorine – Disinfection
  • Sodium Hydroxide – pH Adjustment
slide-25
SLIDE 25

Considerations/Concerns

  • Incomplete reactions
  • Formation of unknown compounds
  • Raw Water Quality Considerations
  • Cost
slide-26
SLIDE 26

Acknowledgements

Calgon Carbon Corporation

slide-27
SLIDE 27

Thank You