nyc watershed/tifft science & technical symposium september 19, 2013
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Treatment of Emerging Environmental Contaminants In Water. NYC Watershed/Tifft Science & Technical Symposium September 19, 2013. Contaminants are now being detected regularly in the water supply - PowerPoint PPT PresentationTRANSCRIPT
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NYC Watershed/Tifft Science & Technical SymposiumSeptember 19, 2013
Treatment of Emerging Environmental Contaminants
In Water
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WATER QUALITY – GLOBAL TRENDS
Contaminants are now being detected regularly in the water supply
Many regulators are now requiring routine testing of chemicals that were virtually unknown just a few years ago
Growing awareness that the water supply is interconnected
Supplies are tightening as population increases and water sources are more heavily tapped
Unintentional water reuse is occurring“One city’s wastewater is another city’s drinking water”
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OUR INTERCONNECTED WATER SUPPLY
Sources of contaminants in our water supply:
- Industrial discharge
- Agricultural runoff
- Chemical releases
- Municipal wastewater
InjectionWell
ExtractionWell
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WHAT IS UV-OXIDATION?
It is the process of destroying trace organic contaminants in water by:
UV-Photolysis UV light alone breaks down the contaminant molecules
UV-OxidationUV light plus hydrogen peroxide (H2O2)
Hydrogen peroxide absorbs UV and produces hydroxyl radicals that oxidize contaminants
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UV-PHOTOLYSIS
Chemical bonds arebroken by UV light
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UV-OXIDATION
Hydrogen peroxide
Hydroxylradical
Chemical bonds arebroken by hydroxyl radicals
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HOW UV TREATS ENVIRONMENTAL CONTAMINANTS
Simultaneous Processes Typically, UV-photolysis and UV-oxidation occur simultaneously: reaction time is milliseconds
Most contaminants are broken down by a combination of both processes
The relative contribution of either UV-photolysis and UV-oxidation varies
by contaminant
The UV energy output for both processes is sufficient to also provide microbial disinfection
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0.0
0.2
0.4
0.6
0.8
1.0
1.2
1.4
1.6
1.8
2.0
7 ppm H2O2 14 ppm H2O2 7 ppm H2O2 14 ppm H2O2 7 ppm H2O2 14 ppm H2O2
Ch
emic
al L
og
Red
uct
ion
per
Un
it o
f P
ow
er D
raw
UV-OxidationUV-Photolysis
TCE
NDMA
1,4-Dioxane
CONTAMINANT DESTRUCTION BALANCE
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EXAMPLES OF ECT CONTAMINANTS
N-nitrosodimethylamine (NDMA)Industrial additive & disinfection byproduct
1,4-DioxaneIndustrial solvent
Pesticides & HerbicidesAgricultural crop protection products
Petroleum AdditivesIncluding MTBE
Volatile Organics (TCE, PCE, Vinyl Chloride, etc.)
Naphthalene and Phenols
Pharmaceuticals & Personal Care ProductsIncludes potential endocrine disruptors
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NDMA AND 1,4-DIOXANE BACKGROUND
• No current federal regulations for either NDMA or 1,4-dioxane, however states have taken actions
• 1,4-dioxane is a solvent stabilizer used to prevent solvent breakdown during degreasing operations
• Conventional treatment technologies such as reverse osmosis (RO), coagulation/filtration, and carbon adsorption are ineffective
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• MTBE is a semi-volatile, chemically unreactive molecule
• Highly soluble in water (increase with Temp decrease),
• Sorbs poorly to soil grains, and has a low volatility (Treat air discharge?)
• Persistent and mobile in groundwater
• Break down to tert-butyl alcohol (TBA)
METHYL TERTIARY BUTYL ETHER (MTBE) - OVERVIEW
Properties of MTBE
Formula C5H12O
Molecular Weight
88.15
Vapor pressure
245 mmHg at 25 ºC
Solubility in water
43,000-50,000 mg/L
Henry’s Law Constant
0.587 L-atm/mol at 25 ºC
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METHYL TERTIARY BUTYL ETHER (MTBE) - OVERVIEW
Oxidation of MTBE generates TBA. TBA adsorbs readily to GAC/BAC
Sources: leaking underground storage tanks, accidental spills of fuels, and releases from recreational vehicles in reservoirs.
Regulated in NY (10 ppb), CA (13 ppb), NH (13 pp), PA (20 ppb), RI (40 ppb) and numerous others
The USEPA has set non-enforceable drinking water advisory levels for MTBE of 20 ppb based on odor and 40 ppb based on taste
Listed on the USEPA’s CCL and UCMR
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Contaminant Quantum Yield
Contaminant - Hydroxyl Radical Rate Constant
Contaminant Molar Absorption Coefficient
Hydrogen Peroxide Concentration
Water Absorbance (UVT)
Water Matrix Hydroxyl Radical Scavenging Capacity
Lamp Type
SIZING FACTORS FOR ECT SYSTEMS
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LAMP TECHNOLOGY
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MPEE/O = 7.92
LPEE/O = 2.85
2.12
2.14
2.16
2.18
2.2
2.22
2.24
2.26
2.28
2.3
2.32
2.34
0 0.2 0.4 0.6 0.8 1 1.2 1.4
Electrical Energy per Volume (kWh/m3)
Lo
g[H
2O
2]
MP Lamp Baseline Condition LP Lamp Baseline Condition
Measured MP:LP = 2.8
LPHO PHOTOLYSIS OF HYDROGEN PEROXIDE
The same number of hydroxyl radicals are produced with ~65% less power for LPHO vs. MP with this water quality
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REACTOR DETAILS
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REACTOR DETAILS LPHO
• Lamp power and number of reactors in operation automatically adjusted to minimize power
• Reactors can be oriented 1-, 2-, or 3-high for small footprint
• 250W LPHO lamp efficiently treating contaminants year round
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Two lamp bundles per chamber (one accessed from each end)
Influent Port
Effluent Port
REACTOR DETAILS LPHO
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Remediation Case Studies
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200 GPM facility treating extracted groundwater
Water is treated through air stripping, then UV-oxidation
Contaminant of concern: 1,4-dioxane, TCE
NDMA reduced from 150 ppb to less than 1 ppb
TrojanUVPhox™, amalgam lamp lamp technology
Full service hydrogen peroxide and delivery and maintenance
GROUNDWATER REMEDIATION INSTALLATION - STOCKTON, CA
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0
50
100
150
200
250
300
1 2 3 4 5 6 7 8 9 10 11 12
Run
1,4
-dio
xan
e C
on
ce
ntr
ati
on
(p
pb
)
Influent
Reactor #1
Reactor #2
1,4-DIOXANE PERFORMANCE TESTING RESULTS - STOCKTON, CA
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Flow: 2378 gpm, 8ppm H2O2 dose
Water is treated through Fe/Mn Filtration
Contaminants of concern: 1,4-dioxane, TCE
1.3 Log reduction of 1,4 dioxane guarantee
GAC for H2O2 quenching/redundancy (change out every 3 years, CL2 dosing back up)
Full service hydrogen peroxide delivery and maintenance
GROUNDWATER TREATMENT INSTALLATION – WATERLOO, ON
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0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
2
1,2,3- 15ppm 1,2,3- Auto 12-18ppm 2,3-18 ppm 1,3-18ppm
Run number and H202 Concentration
1,4
Dio
xa
ne
Lo
g R
ed
uc
tio
n
Guaranteed Log reduction
Actual Log Reduction
1,4-DIOXANE PERFORMANCE TESTING RESULTS – Greenbrook, ON
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LOCATION OF CALIFORNIA DOMESTIC WATER CO
The California Domestic
Treatment Facility
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CONTAMINATION IN THE SAN GABRIEL VALLEY – BACKGROUND
VOCs discovered in 1979
Plume defined, now traverses several “Operable Units” including the Baldwin Park OU
1997, NDMA, 1,4-dioxane and perchlorate detected
Cal Domestic
Plume map courtesy of EPA Region 9 Mailer, May 1999
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Flow Rate: 6.8 MGD (one train of two, =4,700gpm)
1. Ion Exchange
2. UV-Photolysis
3. Air Stripping
4. Chlorination (for residual in distribution system)
THE TREATMENT PROCESS AT CAL DOMESTIC
Medium Pressure Rayox™
October 2001 to April 2005
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Flow Rate: 6.8 MGD (one train of two, =4,700gpm)
1. Ion Exchange
2. UV-Photolysis
3. Air Stripping
4. Chlorination (for residual in distribution system)
THE TREATMENT PROCESS AT CAL DOMESTIC
Low Pressure High Output
TrojanUVPhox™ April 2005 to
Present
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NDMA TREATMENT PERFORMANCE CAL DOMESTIC
0
20
40
60
80
100
120
140
160
05/01/01 05/01/02 05/01/03 04/30/04 04/30/05 04/30/06 04/30/07
Sampling Date
ND
MA
Co
nce
ntr
atio
n (
pp
t)
NDMA, UV Influent
NDMA, UV Effluent
TrojanUVPhox Online
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ENERGY USAGE (kWh) CAL DOMESTIC
-
50,000
100,000
150,000
200,000
250,000
300,000
350,000
400,000
450,000
05/01/01 05/01/02 05/01/03 04/30/04 04/30/05 04/30/06 04/30/07
Date
Mo
nth
ly k
ilo
wat
t-h
ou
r (k
Wh
) U
sag
e
TrojanUVPhox™ Operational
(April 21, 2005)
• ~5X more power used with MP solution vs. LPHO solution• Theory states that the lowest power ratio would be 3X• Increase to 5X from 3X due to enhanced optical & hydraulic efficiencies with LPHO reactor when compared to MP reactor
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OTHER REMEDIATION PROJECTS
El Monte, California – 0.072 MGD (50 gpm)
Secor, Colorado – 0.029 MGD (20 gpm)
Sunnyvale, California – 0.14 MGD (100 gpm)
La Puente Valley County Water District, CA – 3.6 MGD
California Domestic Water Company, CA – 14.5 MGD
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Suffolk County Water Authority Pilot
• Prove technology effectiveness on destruction of 1,4 dioxane and other VOCs
• Existing GAC for removing residual peroxide (extends GAC life)
• Water quality higher than initial design (99% UVT vs 95% UVT)
• Scavenging demand lower = lower H2O2 dose
• 1200 gpm Full scale system in design