POISON!!! In r Water - University of Oklahoma in OU... · Water Supply Paul Gerber Collin Martin...
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POISON!!! POISON!!! In r Water In r Water
http://www.enn.com/news/enn-stories/2001/09/09142001/arsenichands.jpg
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Arsenic Removal from the Arsenic Removal from the University of OklahomaUniversity of Oklahoma
Water SupplyWater Supply
Paul GerberPaul GerberCollin MartinCollin Martin
John SiskaJohn SiskaApril 2004April 2004
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BackgroundBackground
•• OU has high arsenic levels (48 ppb) in OU has high arsenic levels (48 ppb) in wells that need to be treatedwells that need to be treated
•• EPA says limit needs to be 10 ppb by EPA says limit needs to be 10 ppb by January 2006January 2006
•• Current limit is 50 ppbCurrent limit is 50 ppb
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Our PurposeOur Purpose
•• Evaluate effectiveness of alternative Evaluate effectiveness of alternative technologiestechnologies
•• Determine which technology is best suitedDetermine which technology is best suited•• Perform cost evaluation of the best Perform cost evaluation of the best
technologiestechnologies
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The History of ArsenicThe History of ArsenicOccurs naturally in rocks and soil, water, air, and plants and animals.
It can be further released into the environment through natural activities such as volcanic action, erosion of rocks, and forest fires
http://www.webelements.com/webelements/elements/text/As/key.html
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Uses of ArsenicUses of ArsenicPAST
Insecticides
Herbicides
Paints
Dyes
CURRENT
Wood preservative
Production of glass
Electronics
Medicine
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Effects of ArsenicEffects of Arsenic
How Arsenic Enters the Body
•From the food we eat every day•By drinking water containing arsenic or eating food cooked in this water•By breathing air containing it•Arsenic is quickly absorbed into the bloodstream
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Known Health EffectsKnown Health Effects• Thickening and discoloration of the skin• Stomach pain• Nausea, vomiting, and diarrhea (300 to 30,000
ppb)• Numbness in the hands and feet• Direct skin contact may cause redness and
swelling
Large oral doses (above 60,000 ppb in food or water) can cause death
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Where is it?Where is it?
Ryker, S.J., Nov. 2001, Mapping arsenic in groundwater: Geotimes v.46 no.11, p.34-36.
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OUOU’’s Wells with Arsenics Wells with Arsenic
Average Arsenic Content
48 ppb
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CH2M Hill Group ResultsCH2M Hill Group ResultsAssumed City of Norman and OU were one Assumed City of Norman and OU were one entitiyentitiy•• CH2M Hill recommendation does not apply strictly to the CH2M Hill recommendation does not apply strictly to the
University of OklahomaUniversity of Oklahoma•• New Wells and BlendingNew Wells and Blending
–– Capital Investment: $9.2 Capital Investment: $9.2 –– NPC: $35,000,000NPC: $35,000,000
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POE & Associates 2002 ResultsPOE & Associates 2002 Results
•• Purchase all potable water from the City of NormanPurchase all potable water from the City of Norman•• Cost: $100,000 + Water Purchase CostCost: $100,000 + Water Purchase Cost
–– Based on $4.00/1000 GallonsBased on $4.00/1000 Gallons–– Changing water connectionsChanging water connections
•• Potable wellsPotable wells•• City of Norman City of Norman
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Past Engineering Group ResultsPast Engineering Group Results
Civil Engineering Group 2001Civil Engineering Group 2001•• 3 MGPD Ion Exchange3 MGPD Ion Exchange•• Capital Investment: $2,179,000Capital Investment: $2,179,000
–– NPC: $17,079,000NPC: $17,079,000
Chemical Engineering Group 2003Chemical Engineering Group 2003•• 1.6 MGPD Ion Exchange1.6 MGPD Ion Exchange•• Capital Investment: $2,000,000Capital Investment: $2,000,000
–– NPC: $3,100,000NPC: $3,100,000–– Based on $1.14/1000 GallonsBased on $1.14/1000 Gallons
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Sources of WaterSources of Water•• Westheimer Airport (North Campus) WellsWestheimer Airport (North Campus) Wells
–– High in Arsenic (30High in Arsenic (30--50 ppb)50 ppb)–– Must be TreatedMust be Treated–– Very Soft (30 mg/L) WaterVery Soft (30 mg/L) Water
•• OKC (Purchased) WaterOKC (Purchased) Water–– Low in Arsenic, but ExpensiveLow in Arsenic, but Expensive–– Soft (60 mg/L) WaterSoft (60 mg/L) Water
•• South Campus WellsSouth Campus Wells–– Currently Used for IrrigationCurrently Used for Irrigation–– 2 ppb Arsenic2 ppb Arsenic–– Very Cheap, but Very Hard (340 mg/L) WaterVery Cheap, but Very Hard (340 mg/L) Water
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Water Treatment ProcessesWater Treatment Processes
•• Water PurchaseWater Purchase•• NanofiltrationNanofiltration•• MicrofiltrationMicrofiltration•• Polyelectrolyte Enhanced UltrafiltrationPolyelectrolyte Enhanced Ultrafiltration•• Reverse OsmosisReverse Osmosis•• Ion ExchangeIon Exchange
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Water PurchaseWater Purchase
•• Buy potable water Buy potable water directly from OKC at directly from OKC at $0.98 per thousand $0.98 per thousand gallons.gallons.
•• Pay $0.05 per Pay $0.05 per thousand gallons to thousand gallons to transmit this water to transmit this water to OU from OKC through OU from OKC through Norman.Norman.
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Water PurchaseWater Purchase
•• ProsPros–– No Initial InvestmentNo Initial Investment–– No Significant Construction NeededNo Significant Construction Needed
•• ConsCons–– Dependence on OKC and Norman for WaterDependence on OKC and Norman for Water–– High Water CostHigh Water Cost
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Membrane SeparationMembrane Separation
•• A mixture is separatedA mixture is separated•• Allows one component to move through faster than othersAllows one component to move through faster than others•• Separated into a retentive and a permeate streamSeparated into a retentive and a permeate stream
Retentive (Waste Water)
Permeate (Treated Water)
Feed Water
Membrane
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Nanofiltration, Microfiltration and Nanofiltration, Microfiltration and UltrafiltrationUltrafiltration
Restricted diffusion
•• Nanofiltration membranes are Nanofiltration membranes are capable of removing arsenate capable of removing arsenate because of their small pore size.because of their small pore size.
•• MicrofiltrationMicrofiltration’’ss pore size is too large pore size is too large to remove arsenate. to remove arsenate.
•• UltrafiltrationUltrafiltration’’ss membrane pore sizes membrane pore sizes are small enough to block the are small enough to block the polymer that is bounded to the polymer that is bounded to the arsenate.arsenate.
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Polyelectrolyte Enhanced Polyelectrolyte Enhanced UltrafiltrationUltrafiltration•• Polymers (longPolymers (long--chain molecules) with a cationic (positive chain molecules) with a cationic (positive
charge) head groupcharge) head group•• Water solubleWater soluble
•• Biodegrade easilyBiodegrade easily
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Polyelectrolyte Enhanced Polyelectrolyte Enhanced UltrafiltrationUltrafiltration •• The polymer used is a The polymer used is a
polyelectrolyte of opposite polyelectrolyte of opposite charge to the target ion charge to the target ion (Arsenate).(Arsenate).
•• Pollutant ions bind to the Pollutant ions bind to the polymerpolymer–– Electrostatic attraction Electrostatic attraction
•• Polymer complexes are retained Polymer complexes are retained by the membrane in the waste by the membrane in the waste stream.stream.
•• UncomplexedUncomplexed ions (water ions (water molecules) pass through the molecules) pass through the membrane to the treated membrane to the treated stream.stream.
•• But polymer is expensiveBut polymer is expensive……H2AsO4
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Reverse OsmosisPressure
Membrane
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Reverse OsmosisReverse Osmosis
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Reverse OsmosisReverse Osmosis
•• ProsPros–– No Chemicals Needed for Normal OperationNo Chemicals Needed for Normal Operation–– Low Maintenance, Easy to OperateLow Maintenance, Easy to Operate
•• ConsCons–– Very Expensive (Membrane)Very Expensive (Membrane)–– High Pumping CostsHigh Pumping Costs–– Creates a lot of Waste (Reject Water)Creates a lot of Waste (Reject Water)
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Ion ExchangeIon Exchange
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Ion ExchangeIon Exchange
•• ProsPros–– Inexpensive to StartInexpensive to Start--Up and OperateUp and Operate–– Removes Virtually All Arsenic from the WaterRemoves Virtually All Arsenic from the Water
•• ConsCons–– Resin must be Regenerated/ReplacedResin must be Regenerated/Replaced–– Risk of Arsenic BreakthroughRisk of Arsenic Breakthrough–– Produces a lot of Waste (but much less than RO)Produces a lot of Waste (but much less than RO)
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Detailed CalculationsDetailed Calculations
•• Water Systems IntegrationWater Systems Integration•• Economic Analysis of Treatment OptionsEconomic Analysis of Treatment Options•• Basis of Calculations (unless otherwise Basis of Calculations (unless otherwise
specified):specified):–– 0.75 MGPD (520 gpm) Potable Demand Today0.75 MGPD (520 gpm) Potable Demand Today–– 1% Annual Growth in Water Demand1% Annual Growth in Water Demand–– 1% Inflation1% Inflation–– 5% Discounting for Net Present Cost Calculations5% Discounting for Net Present Cost Calculations
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Water Systems IntegrationWater Systems Integration
•• North Campus Treatment Facility North Campus Treatment Facility IntegrationIntegration
•• South Campus Well IntegrationSouth Campus Well Integration
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OptionsOptions
1.1. Buying all water from OKC (WP)Buying all water from OKC (WP)2.2. Treating all north campus water (IX)Treating all north campus water (IX)3.3. Blending treated water with south Blending treated water with south
campus water (IX + SC)campus water (IX + SC)4.4. Blending purchased water with Blending purchased water with
south campus water (WP + SC)south campus water (WP + SC)5.5. Treating South Campus Water Treating South Campus Water
Directly for HardnessDirectly for Hardness
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Water Sources and Costs Water Sources and Costs per 1000 gallonsper 1000 gallons
•• $1.030 $1.030 OKCOKC•• $0.791$0.791 Ion ExchangeIon Exchange•• $0.085$0.085 South Campus
O.U.
North Campus
OKC
South Campus
South Campus
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North CampusNorth Campus
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North CampusNorth Campus# Parts Cost/Part Total Cost
Facility 1 $300,000 $300,000Pum ps 2 $15,200 $30,400
G ate valves 5 $2,700 $13,500Relief valve 1 $525 $525
Check valves 3 $1,650 $4,950M eters 2 $5,100 $10,200
M eter vault 1 $3,200 $3,200Elbow s 90 7 $315 $2,205
T connectors 4 $475 $1,900Pipe SCD 80 (1 foot) 8" 400 $36 $14,400
Variable Drives 2 $7,500 $15,000Controllers 2 $2,000 $4,000
Total $400,280
O perating Expenses Cost ($/yr)
Pum p Pow er $23,389Utilities $1,700
Total: $25,089
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South Campus Wells South Campus Wells 2, 10 and 112, 10 and 11
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South Campus WellsSouth Campus Wells
•• 11 Wells Total, with 11 Wells Total, with FlowratesFlowrates of 12 of 12 –– 282 gpm282 gpm
Well 1 2 3 4 5 6 7 8 9 10 11GPM 16 160 25 50 55 16 50 35 12 218 282
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DEQ Test Results S.C. Well 10DEQ Test Results S.C. Well 10
Test Ran
Total Alkalinity
g/LTDS mg/L
Nitrates mg/L
Hardness mg/L
Chloride mg/L
Sulfite mg/L
Conductance UMHOS/cm Ph
Arsenic ppb
Test Results 337 418 1.44 342 10 25.1 743 7.28 2Limits None 500 10 None 250 150 None 6.5 - 8.5 10
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South Campus Wells: 2, 10, & 11South Campus Wells: 2, 10, & 11
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Cost of Integrating South campusCost of Integrating South campus
C 901 8" PVC PIPE in feet 10032 $19.10 191611.2Tee 2 $340.00 68090 Elbow 5 $209.00 1045Pipe and FittingsTrenching in feet 10032 $0.85 8527.2Meter 1 $5,075.00 5075Vault 1 $3,700.00 3700Re-classifying wells 3 $500.00 1500Up-grading wells 3 $1,000.00 3000
Total $215,138
Operating Expenses Cost ($/yr)Maintenance $4,500.00Pump Power Wells $21,204.00
Total $25,704.00
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However, Using the South Campus Wells However, Using the South Campus Wells Increases Irrigation CostsIncreases Irrigation Costs
•• Due to deeper wells and royaltiesDue to deeper wells and royalties•• Increases cost by $0.31/1000 galIncreases cost by $0.31/1000 gal•• Maximum cost per year $46,872Maximum cost per year $46,872•• Minimum cost per year $33,480Minimum cost per year $33,480•• Average Value per year $40,176Average Value per year $40,176
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Augmenting with South CampusAugmenting with South Campus
SourceCost/1000
gallonAverage Cost
50-50%Average
Cost 66-33%Oklahoma city $1.030 $0.558 $0.715Ion Exchange $0.791 $0.438 $0.556South Campus Wells 2,10,11 $0.085
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University Water Cost University Water Cost 150 mg/L Hardness150 mg/L Hardness
Year
500 gpm purchase
CostPurchase /
S.C 66/33%Savings per Year
IX / S.C . 66/33%
Savings w ith IX &
S.C.1 $281,944 $195,523 $86,421 $146,300 $135,6445 $305,305 $211,723 $93,582 $158,422 $146,883
10 $337,247 $233,874 $103,373 $174,997 $162,25015 $372,530 $258,342 $114,188 $193,305 $179,22520 $411,505 $285,371 $126,134 $213,529 $197,976
Year
1000 gpm purchase
CostPurchase / S.C 66/33%
Savings per Year
IX / S.C. 66/33%
Savings with IX &
S.C.1 $541,368 $375,428 $165,940 $280,915 $260,4535 $586,224 $406,535 $179,689 $348,598 $323,20710 $647,556 $449,067 $198,488 $456,577 $423,32015 $715,305 $496,050 $219,255 $598,001 $554,44320 $790,141 $547,948 $242,194 $783,232 $726,182
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Water Cost Mixing 33% of Water Cost Mixing 33% of South Campus WellsSouth Campus Wells
Water Consumption 520 gpm
$0
$50,000
$100,000
$150,000
$200,000
$250,000
$300,000
$350,000
$400,000
$450,000
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20
Time in Years
Cost
per
yea
r
100% Purchase33% mix of S.C.33%S.C. 66% I / X
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4343
University Water Cost University Water Cost 200 mg/L Hardness200 mg/L Hardness
Y ear
500 gpm purchase
C ost
P urchase/ S .C .
50/50%Sav ings per Y ear
IX / S .C . 50/50%
Sav ings IX / S .C .
1 $281,944 $152,606 $129,338 $119,895 $162,0495 $305,305 $165,250 $140,055 $129,829 $175,476
10 $372,530 $182,539 $154,708 $143,412 $193,83515 $372,530 $201,636 $170,894 $158,416 $214,11420 $411,505 $222,732 $188,773 $174,989 $236,515
Year
1000 gpm purchase
Cost
Purchase/ S.C.
50/50%Savings per Year
IX / S.C. 50/50%
Savings IX / S.C.
1 $541,368 $293,022 $248,346 $230,213 $311,1555 $586,224 $317,301 $268,923 $285,680 $386,125
10 $715,305 $350,498 $297,058 $374,170 $505,72715 $715,305 $387,167 $328,137 $490,068 $662,37620 $790,141 $428,803 $361,338 $641,867 $867,546
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4444
Water Cost Mixing 50% of Water Cost Mixing 50% of South Campus Wells South Campus Wells
Water Consumption 520 gpm
$0
$50,000
$100,000
$150,000
$200,000
$250,000
$300,000
$350,000
$400,000
$450,000
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20
Time in years
Cos
t per
yea
r
100% Purchase50% mix with S.C. 50% S.C. and 50% I / X
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4545
North/South Campus Time LineNorth/South Campus Time Line
Time inTime inMonthsMonths
Steps in ProcessSteps in Process
33 Initiating ProposalInitiating Proposal33 Prepare and Present to RegentsPrepare and Present to Regents
33 Selection for Bid ProcessSelection for Bid Process
33 ReRe--Submission to RegentsSubmission to Regents
1818 Construction Complete afterConstruction Complete afterRegents ApprovalRegents Approval
3030 Total TimeTotal Time
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4646
Treating South Campus Water Treating South Campus Water Hardness DirectlyHardness Directly
•• Use Ion ExchangeUse Ion Exchange–– Most widely used method of hardness Most widely used method of hardness
correctioncorrection–– Much cheaper than membrane processesMuch cheaper than membrane processes–– Cationic Exchange ResinCationic Exchange Resin–– Will attract ions such as calcium and Will attract ions such as calcium and
magnesiummagnesium–– Use of NaCl or Use of NaCl or KClKCl for treatmentfor treatment
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4747
Treating Water HardnessTreating Water Hardness
•• 342 mg/L of hardness342 mg/L of hardness–– 160 mg/L of sodium160 mg/L of sodium–– For every liter (0.26 gallon) of water intake, For every liter (0.26 gallon) of water intake,
there would be 160 mg of sodium intakethere would be 160 mg of sodium intake–– 1 cup of skim milk has about 125 mg sodium 1 cup of skim milk has about 125 mg sodium –– Concerns about dietConcerns about diet
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4848
Options for Water HardnessOptions for Water Hardness
Potassium chloride as an alternativePotassium chloride as an alternative
Does not damage vegetation, it is good for Does not damage vegetation, it is good for human consumption in the treated waterhuman consumption in the treated water
Waste does not have to go to the waste Waste does not have to go to the waste treatment plant.treatment plant.
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4949
Treating Water Hardness DirectlyTreating Water Hardness Directly
•• $11.7M Net Present Cost$11.7M Net Present Cost•• Economically UnattractiveEconomically Unattractive
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5050
Economics of Water TreatmentEconomics of Water Treatment
•• Net Present Worth Treatment Process Net Present Worth Treatment Process Comparison Comparison
•• Fixed Investment ComparisonFixed Investment Comparison•• Operating Cost ComparisonOperating Cost Comparison•• Uncertainty AnalysisUncertainty Analysis•• ConclusionsConclusions
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5151
Net Present Costs of Different Treatment Options
0
1
2
3
4
5
6
7
8
IX RO WP IX + SC50:50
RO + SC50:50
WP + SC50:50
Treatment Option
Net
Pre
sent
Cos
t (M
illio
ns o
f $)
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5252
Comparison of Fixed Investments
0.0
0.5
1.0
1.5
2.0
2.5
3.0
IX RO WP IX + SC50:50
RO + SC50:50
WP + SC50:50
Treatment Option
Fixe
d In
vest
men
t (M
illio
ns o
f $)
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5353
Operating Cost vs. Operating Flow Rate
$0$100,000$200,000$300,000$400,000$500,000$600,000$700,000$800,000$900,000
0.0 0.5 1.0 1.5 2.0
Average Potable Water Demand (MGPD)
Ope
ratin
g C
ost (
$/yr
)
Ion ExchangeReverse OsmosisWater Purchase
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5454
Project Cost Timeline
$0
$200,000
$400,000
$600,000
$800,000
$1,000,000
$1,200,000
Constu
ction 2 4 6 8 10 12 14 16 18 20
Time (years)
Cos
t
IX + SC Costs
WP + SC Costs
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5555
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
$0 $2,000,000 $4,000,000 $6,000,000 $8,000,000
Cost ($)
Cum
ulat
ive
Prob
abili
ty
a
Water Purchase + South Campus WellsIon Exchange + South Campus Wells
Uncertainty AnalysisUncertainty Analysis
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5656
Conclusion Depends on Recommendation, HoweverConclusion Depends on Recommendation, However……
0
2
4
6
8
10
12
14
0 0.5 1 1.5 2
Current Potable Water Demand (MGPD)
Cos
t (M
illio
ns o
f $)
Ion Exchange + South Campus
Water Purchase + SouthCampus
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5757
ConclusionsConclusions
•• Blend South Campus Water with Purchased Water at low Blend South Campus Water with Purchased Water at low (<1.25 MGPD) Current Water Demands(<1.25 MGPD) Current Water Demands
•• Using Ion Exchange with South Campus Water for higher Using Ion Exchange with South Campus Water for higher (>1.25 MGPD) Current Water Demands(>1.25 MGPD) Current Water Demands
•• Use 50:50 Blending Ratio to Achieve 200 mg/L Hardness Use 50:50 Blending Ratio to Achieve 200 mg/L Hardness (Moderately Hard)(Moderately Hard)
•• Resulting Water will be 5 ppb in ArsenicResulting Water will be 5 ppb in Arsenic
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5858
Questions?Questions?
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5959
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6060
Appendix SlidesAppendix Slides
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6161
Ion Exchange Fixed Charges
$255,474.00, 23.7%
$227,432.94, 21.1%
$5,229.00, 0.5%
$5,976.00, 0.6%
$162,230.00, 15.1%
$18,754.40, 1.7%$1,040.21, 0.1%
$400,280.00, 37.2%
Columns Cost/Installation:
Storage TanksCost/Installation:
NaCl Initial Cost (to first makeup brine):Instrumentation and Controls:
Piping and Valves:
Brine/NaOCl PumpsPurchase/Installation:
Resin Purchase Cost:
Process Integration/FacilityCosts:
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6262
Ion Exchange Operating Costs (at 1.0 MGPD)$9,262.02, 3.3%
$3,193.31, 1.1%
$20,440.00, 7.3%
$49,683.58, 17.8%
$61,116.13, 21.9%
$92,118.06, 33.0%
$25,089.00, 9.0%
$18,250.00, 6.5%NaCl Annual Cost (to maintainbrine):NaOCl Annual Purchase Cost:
Labor/Maintainence Costs:
Sewage Disposal Cost:
Royalties:
Pump Electricity Costs:
Process Integration/FacilityCosts:City of Norman TransmissionCosts:
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6363
Revese Osmosis Fixed Charges
$59,480.00, 2.7%
$1,700,000.00, 77.1%
$36,645.00, 1.7%
$9,177.20, 0.4%
$400,280.00, 18.1%
RO System Purchase/Installation:
Instrumentation and Controls:
Piping and Valves:
Pump Purchase/Installation:
Process Integration/Facility Costs:
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6464
Reverse Osmosis Operating Costs (at 1.0 MGPD)
$109,500.00, 26.7%
$35,587.50, 8.7%
$20,440.00, 5.0%
$18,250.00, 4.4%
$25,089.00, 6.1%
$201,937.18, 49.2%
Pump Electricity Costs:
Royalties:
Maintainence:
Labor:
City of NormanTransmission Costs:ProcessIntegration/Facility Costs:
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6565
After Investment Water Costs
$0.00
$0.50
$1.00
$1.50
$2.00
$2.50
0 2 4 6 8 10 12 14 16 18 20
Timeline after Construction (yrs.)
Cos
t ($/
1000
gal
.)
Ion ExchangeReverse OsmosisWater Purchase
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6666
After Investment Water Costs
$0.00
$0.20
$0.40
$0.60
$0.80
$1.00
$1.20
$1.40
$1.60
$1.80
0 2 4 6 8 10 12 14 16 18 20
Timeline after Construction (yrs.)
Cos
t ($/
1000
gal
.)
IX + SCRO + SCWP + SC
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6767
PEUF Fixed Capital Costs
Engineering and Supervision:, $6,506
Piping and Valve Total Cost, $9,900
Instrumentation and Controls Total Cost,
$12,500
UF System Purchase/Installation,
$39,430
Pump Purchase, Filters, and Accessories Total
Cost, $93,242
UF System Purchase/Installation
Instrumentation and Controls TotalCostPiping and Valve Total Cost
Engineering and Supervision:
Pump Purchase, Filters, andAccessories Total Cost
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6868
PEUF Operating Costs
Raw Materials, $722,470
Maintanence, $82,125
Royalties, $41,090Annual Labor Cost ($/yr),
$81,760
Pump Electricity Costs, $8,763
Royalties
Maintanence
Raw Materials
Pump Electricity Costs
Annual Labor Cost ($/yr)