Desalination Overview
What Are Our Options?
Arizona Water Initiative
Desalination Committee Meeting
September 20, 2016
Zacary Richards
2
Discussion Topics
Current & Potential
Saline Water Projects
Current & Potential
Ocean Water Projects
3
Current Saline Water Projects
What Has Been Done?
Current Saline Water Projects
What Has Been Done?
4
Scottsdale Water Campus Advanced Water
Treatment Facility
 Began production in 1999
 The RO system capacity increased from 13.8 MGD
to 20 MGD using a large-diameter (16 in.) RO
system to save space.
 20 MGD of ultrapure recycled water for use in
blending with CAP water and effluent for both
groundwater recharge and golf course irrigation
 Addresses contaminant removal, including N-
nitrosodimethylamine (chlorination byproduct)
and other unregulated compounds, using a
combination of ozonation, chloramination, and
ultraviolet (UV) technology.
 Brine concentrate is discharged into the 91st
Avenue Wastewater Treatment Plant
5
Current Saline Water Projects
What Has Been Done?
Goodyear Reverse Osmosis (RO) Facility
 Centerra Well contains 1,900 mg/L of Total
Dissolved Solvents (TDS) and 17.9 mg/L of
Nitrate
 3.2 MGD of brackish water is sent from
the well to the RO Facility
 Facility treats 2.7 MG of well water and
provides 2 mg of clean drinking water
which is mixed with .5 MG of brackish
water
 The .7 MG of brine concentrate (7,447
mg/L TDS) is mixed with wastewater,
cleaned to an A+ quality at the 157th Ave
water reclamation plant, and stored
underground
 Capital Cost: $1.98M
 Operating Cost: $0.93/kgal
6
Current Saline Water Projects
What Has Been Done?
Bullard Water Campus
 A permanent facility to replace the
emergency facility in Goodyear
 Water capacity of approximately 5 MGD
and began operation in early 2008
 15,500 square foot prefabricated building
including:
 Eight RO skids
 Sulfuric acid chemical treatment system
 Threshold inhibitor system
 Caustic soda chemical treatment system
 Chlorine system
 Clean in place system
 Sewer discharge tank
 SCADA operating and monitoring system, and site
enhancements
Capital Cost: $10,789,745
Current Saline Water Projects
What Has Been Done?
7
Bullard Water Campus
 Wetlands brine treatment would reduce the
volume of salt entering the 157th Ave water
reclamation facility.
 This will lower the salt content in reclaimed
water. More landscaped facilities may be
willing to use reclaimed water with lower salt
content.
 Lower salt content would reduce facility
operating costs through improved efficiency.
 Wetlands brine treatment will save energy.
 Wetlands brine treatment would require less
energy than other disposal alternatives for
brine.
Methods of Brine Disposal
8*million gallons per day
Central Arizona Salinity Study 2010
Current Saline Water Projects
What Has Been Done?
9
Yuma Desalting Plant (YDP)
 Completed in 1992 to treat saline
agricultural drainage from the Wellton-
Mohawk Irrigation District until it became
dormant
 Bureau of Reclamation conducted a year-
long pilot test from May 2010 to March
2011 and treated 30,496 acre-feet of
drainage water (~27.2 MGD) at 1/3 of the
plant’s capacity
 Power Consumption: 37,541 MWh with an
average price of $32.68 per MWh
 82% efficiency if operated at 430 psi, but
higher power costs
 Produced water had an average salt
concentration of 252 mg/L TDS
Final Pilot Run Report
Reclamation, 2012
Current Saline Water Projects
What Has Been Done?
10
Yuma Desalting Plant (YDP)
Trial Costs
*lower than expected costs for power, labor,
chemicals and materials
Final Pilot Run Report
Reclamation, 2012
Future Brackish Water Projects
What Can We Do?
11 Final Pilot Run
Report
Reclamation, 2012
Future Saline Water Projects
What Can We Do?
12
Yuma Brackish Groundwater
Treatment of Yuma Mesa
 USGS estimates 600,000 to 800,000
acre-feet of brackish groundwater
 Estimated yield: 40,000 AFY
 Capital Cost: $132M
 Annual O&M: $1.7M
 Implementation: 7-9 yrs
Black & Veatch 2014
Yuma Desalination Plant
Well Field
Future Saline Water Projects
What Can We Do?
13
Navajo/Hopi Planning Area
 Saline groundwater due to bedded salt
in sedimentary formations
 Little Colorado and Eight Lakes in the PA
have impaired water quality due to
levels of turbidity, lead, copper, mercury
and silver in excess of use standards
 Municipalities are projected to consume
23,093 acre feet per year by 2035
Phoenix AMA Basin
 A 35 mile long brackish water supply
exists on the Gila River between its
confluence with the Salt River to the
outfall of the Basin at Gillispie Dam
Future Saline Water Projects
What Can We Do?
14
Future Saline Water Projects
What Can We Do?
15
Desalination in California
Imperial Valley Drain Water Treatment
 Yield = 200,000 AFY increments
 Capital Cost = $2.25B
 Annual O&M = $77M
 Unit Cost = $1,000/AF
 Implementation = ~ 15 years
Black & Veatch 2014
Coachella Valley Drain Water Treatment
 Yield = 101,000 AFY
 Capital Cost = $395M
 Annual O&M = $30M
 Unit Cost = $500/AF
 Implementation = ~15 years
Key Factors:
• Dust Control
• Reduced Flows to Salton Sea
• Migratory Bird Impacts
Current Ocean Water Projects
What Has Been Done?
16
Carlsbad Desalination Plant
 2,000 pressure vessels with 8 RO membranes
in each vessel
 Draws 100 MGD of ocean water and produces
50 MGD or 7% of San Diego’s water supply
(enough for 112,000 households)
 Two stage pretreatment process
 Microfiltration
 Multimedia Filtration Tanks
 Energy recovery devices recycle 46% of
energy used in the RO process saving $12m
annually
 40MW to operate which is energy for 30,000
homes and costs $49m-$59m annually
 $2000 - $2200 per acre foot or an increase of
$5 - $7 on monthly water bills
 Capital Cost: $734m in private bonds
 15 year process
Future Ocean Water Projects
What Can We Do?
17
Sea of Cortez Desalination
 Treated water could be conveyed via
pipeline and discharged upstream of
Morelos Dam
 RO rejected brine would be deposited into
the Sea of Cortez
 Water could be delivered to Mexico in
exchange for upstream storage or
diversion
 Estimated Yield: 200,000 to 1.3M AFY
 Capital Cost: $4.5B
 Annual O&M: $185M
 Unit Cost: $2,200/AF
 Implementation: 15 yrs
Colorado River Delta Biosphere Reserve
Pincate and Gran Desierto de Altar Biosphere Reserve
Black & Veatch 2014
Things to Consider
18
Membrane Upgrades
 Reducing energy costs by using
graphene, which is one atom thick,
instead of polyamide
 Use 16 inch diameter membranes
instead of 8 inch diameter – more
surface area and less energy cost,
however, only one manufacturer
makes them
Dilution Solution
 Using reverse osmosis pressure
retarded osmosis (RO-PRO) results
in a decrease in energy by 30%
http://www.pri.org/stories/2015-05-15/desalination-expensive-energy-hog-improvements-are-way
Things to Consider
19
http://www.pri.org/stories/2015-05-15/desalination-expensive-energy-hog-improvements-are-way
Recapturing and Renewable
 Turbochargers take kinetic energy from
the output and reapply it to the input
 Pretreating water before it goes into
the membranes saves energy and the
life of the membranes
Environmental Concerns
 RO-PRO reduces salt concentration in
the discharge
 Forward osmosis in smaller plants that
produce no more than 26,000 gallons
of water a day see a 42% reduction in
energy use
 Diffusers increase the volume of
seawater mixing with the concentrated
discharge and prevents spots on the
ocean floor containing high salt levels
Things to Consider
20
http://www.pri.org/stories/2015-05-15/desalination-expensive-energy-hog-improvements-are-way
Membrane Capacitive Deionization (MCDI)
 Separates ions using electrodes
 318,000 gallons per day plant in China
 75% water recovery rate
 1kWh for 264 gallons = $0.22
Questions?
Arizona Water Initiative
Coordinator:
Zacary Richards
zbrichards@azwater.gov
(602) 771-8311

DesalinationPresentation

  • 1.
    Desalination Overview What AreOur Options? Arizona Water Initiative Desalination Committee Meeting September 20, 2016 Zacary Richards
  • 2.
    2 Discussion Topics Current &Potential Saline Water Projects Current & Potential Ocean Water Projects
  • 3.
    3 Current Saline WaterProjects What Has Been Done?
  • 4.
    Current Saline WaterProjects What Has Been Done? 4 Scottsdale Water Campus Advanced Water Treatment Facility  Began production in 1999  The RO system capacity increased from 13.8 MGD to 20 MGD using a large-diameter (16 in.) RO system to save space.  20 MGD of ultrapure recycled water for use in blending with CAP water and effluent for both groundwater recharge and golf course irrigation  Addresses contaminant removal, including N- nitrosodimethylamine (chlorination byproduct) and other unregulated compounds, using a combination of ozonation, chloramination, and ultraviolet (UV) technology.  Brine concentrate is discharged into the 91st Avenue Wastewater Treatment Plant
  • 5.
    5 Current Saline WaterProjects What Has Been Done? Goodyear Reverse Osmosis (RO) Facility  Centerra Well contains 1,900 mg/L of Total Dissolved Solvents (TDS) and 17.9 mg/L of Nitrate  3.2 MGD of brackish water is sent from the well to the RO Facility  Facility treats 2.7 MG of well water and provides 2 mg of clean drinking water which is mixed with .5 MG of brackish water  The .7 MG of brine concentrate (7,447 mg/L TDS) is mixed with wastewater, cleaned to an A+ quality at the 157th Ave water reclamation plant, and stored underground  Capital Cost: $1.98M  Operating Cost: $0.93/kgal
  • 6.
    6 Current Saline WaterProjects What Has Been Done? Bullard Water Campus  A permanent facility to replace the emergency facility in Goodyear  Water capacity of approximately 5 MGD and began operation in early 2008  15,500 square foot prefabricated building including:  Eight RO skids  Sulfuric acid chemical treatment system  Threshold inhibitor system  Caustic soda chemical treatment system  Chlorine system  Clean in place system  Sewer discharge tank  SCADA operating and monitoring system, and site enhancements Capital Cost: $10,789,745
  • 7.
    Current Saline WaterProjects What Has Been Done? 7 Bullard Water Campus  Wetlands brine treatment would reduce the volume of salt entering the 157th Ave water reclamation facility.  This will lower the salt content in reclaimed water. More landscaped facilities may be willing to use reclaimed water with lower salt content.  Lower salt content would reduce facility operating costs through improved efficiency.  Wetlands brine treatment will save energy.  Wetlands brine treatment would require less energy than other disposal alternatives for brine.
  • 8.
    Methods of BrineDisposal 8*million gallons per day Central Arizona Salinity Study 2010
  • 9.
    Current Saline WaterProjects What Has Been Done? 9 Yuma Desalting Plant (YDP)  Completed in 1992 to treat saline agricultural drainage from the Wellton- Mohawk Irrigation District until it became dormant  Bureau of Reclamation conducted a year- long pilot test from May 2010 to March 2011 and treated 30,496 acre-feet of drainage water (~27.2 MGD) at 1/3 of the plant’s capacity  Power Consumption: 37,541 MWh with an average price of $32.68 per MWh  82% efficiency if operated at 430 psi, but higher power costs  Produced water had an average salt concentration of 252 mg/L TDS Final Pilot Run Report Reclamation, 2012
  • 10.
    Current Saline WaterProjects What Has Been Done? 10 Yuma Desalting Plant (YDP) Trial Costs *lower than expected costs for power, labor, chemicals and materials Final Pilot Run Report Reclamation, 2012
  • 11.
    Future Brackish WaterProjects What Can We Do? 11 Final Pilot Run Report Reclamation, 2012
  • 12.
    Future Saline WaterProjects What Can We Do? 12 Yuma Brackish Groundwater Treatment of Yuma Mesa  USGS estimates 600,000 to 800,000 acre-feet of brackish groundwater  Estimated yield: 40,000 AFY  Capital Cost: $132M  Annual O&M: $1.7M  Implementation: 7-9 yrs Black & Veatch 2014 Yuma Desalination Plant Well Field
  • 13.
    Future Saline WaterProjects What Can We Do? 13 Navajo/Hopi Planning Area  Saline groundwater due to bedded salt in sedimentary formations  Little Colorado and Eight Lakes in the PA have impaired water quality due to levels of turbidity, lead, copper, mercury and silver in excess of use standards  Municipalities are projected to consume 23,093 acre feet per year by 2035 Phoenix AMA Basin  A 35 mile long brackish water supply exists on the Gila River between its confluence with the Salt River to the outfall of the Basin at Gillispie Dam
  • 14.
    Future Saline WaterProjects What Can We Do? 14
  • 15.
    Future Saline WaterProjects What Can We Do? 15 Desalination in California Imperial Valley Drain Water Treatment  Yield = 200,000 AFY increments  Capital Cost = $2.25B  Annual O&M = $77M  Unit Cost = $1,000/AF  Implementation = ~ 15 years Black & Veatch 2014 Coachella Valley Drain Water Treatment  Yield = 101,000 AFY  Capital Cost = $395M  Annual O&M = $30M  Unit Cost = $500/AF  Implementation = ~15 years Key Factors: • Dust Control • Reduced Flows to Salton Sea • Migratory Bird Impacts
  • 16.
    Current Ocean WaterProjects What Has Been Done? 16 Carlsbad Desalination Plant  2,000 pressure vessels with 8 RO membranes in each vessel  Draws 100 MGD of ocean water and produces 50 MGD or 7% of San Diego’s water supply (enough for 112,000 households)  Two stage pretreatment process  Microfiltration  Multimedia Filtration Tanks  Energy recovery devices recycle 46% of energy used in the RO process saving $12m annually  40MW to operate which is energy for 30,000 homes and costs $49m-$59m annually  $2000 - $2200 per acre foot or an increase of $5 - $7 on monthly water bills  Capital Cost: $734m in private bonds  15 year process
  • 17.
    Future Ocean WaterProjects What Can We Do? 17 Sea of Cortez Desalination  Treated water could be conveyed via pipeline and discharged upstream of Morelos Dam  RO rejected brine would be deposited into the Sea of Cortez  Water could be delivered to Mexico in exchange for upstream storage or diversion  Estimated Yield: 200,000 to 1.3M AFY  Capital Cost: $4.5B  Annual O&M: $185M  Unit Cost: $2,200/AF  Implementation: 15 yrs Colorado River Delta Biosphere Reserve Pincate and Gran Desierto de Altar Biosphere Reserve Black & Veatch 2014
  • 18.
    Things to Consider 18 MembraneUpgrades  Reducing energy costs by using graphene, which is one atom thick, instead of polyamide  Use 16 inch diameter membranes instead of 8 inch diameter – more surface area and less energy cost, however, only one manufacturer makes them Dilution Solution  Using reverse osmosis pressure retarded osmosis (RO-PRO) results in a decrease in energy by 30% http://www.pri.org/stories/2015-05-15/desalination-expensive-energy-hog-improvements-are-way
  • 19.
    Things to Consider 19 http://www.pri.org/stories/2015-05-15/desalination-expensive-energy-hog-improvements-are-way Recapturingand Renewable  Turbochargers take kinetic energy from the output and reapply it to the input  Pretreating water before it goes into the membranes saves energy and the life of the membranes Environmental Concerns  RO-PRO reduces salt concentration in the discharge  Forward osmosis in smaller plants that produce no more than 26,000 gallons of water a day see a 42% reduction in energy use  Diffusers increase the volume of seawater mixing with the concentrated discharge and prevents spots on the ocean floor containing high salt levels
  • 20.
    Things to Consider 20 http://www.pri.org/stories/2015-05-15/desalination-expensive-energy-hog-improvements-are-way MembraneCapacitive Deionization (MCDI)  Separates ions using electrodes  318,000 gallons per day plant in China  75% water recovery rate  1kWh for 264 gallons = $0.22
  • 21.
  • 22.