a portable and battery-powered seawater … institute of technology research laboratory of...
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Massachusetts Institute of Technology Research Laboratory of Electronics
A Portable and Battery-Powered Seawater Desalination Device by
Ion Concentration Polarization
Dr. Sung Jae Kim,Prof. Jongyoon Han
November 16, 2010November 16, 2010
Micro/Nanofluidic BioMEMS Group,Department of Electrical Engineering and Computer Science,
Massachusetts Institute of Technology Research Laboratory of Electronics
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Water Resource on the Earth
World Water Development Report
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Global Water Market
Source: Global water Intelligence: Global Water Market 2008
9%7.3Desalination plants running operation8%2.4Desalination plants with membrane4%2.5Thermal desalination plants
Desalination20%1.9Treatment using membrane systems
14%0.5UV treatment
10%0.3Ozone treatment(10%)(91)(Sales of bottled water)
4%129Drinking water purification
Drinking water
19%4.2Membrane systems for wastewater treatment
4%13Chemicals and services for the industry
6%12Equipment for wastewater treatment
4%104Sewage treatment
Wastewater
Expected annual growth
Market volume 2007 (USD bn)
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Fresh Water in Resource-Limited Setting
Disaster-stricken areas
www.sacbee.com
Worldwide use of improved sanitation facilities in 2008WHO report 2010
2.6 billion people do not use improved sanitationBrackish ground water
www.who.int
Groundwater turns brackish
Disaster relief, military and humanitarian operation
Underdeveloped area
www.un.org
Lack of delivery and on-grid infrastructures
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www.watertechnology.net
Conventional Seawater Desalination
• Best energy efficiency ~ 5 Wh/L
• Requires large scale plants and significant membrane fouling
Thermal distillation / freezing
• Easiest method
• Energetically costly
Reverse Osmosis
• Less membrane fouling
• Worse energy efficient ~ 20 Wh/L
Electro-Dialysis
www.thewatertreatments.com
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Competing Technologies
Small/Medium scale desalination / purification system
• Household RO machine with UV lamps only for tap water like groundwatere.g. Aquaguard®, GE profileTM (only for <2000ppm TDS source water)
c.f. Brackish water: 1000-5000ppm TDS, Seawater: 30,000-40,000ppm TDS
• Medium-scale seawater desalination RO systems are not cost- and energy-efficiente.g. Ampac Seapro 100 (>$7650), 30-90Wh/L
• Other technologies focusing on particulate/organics, not salte.g. spiral filtration system (PARC)
chemical agent for inducing flocculation-sedimentationactivated carbon filters
Organism Examples General Size Filter Type Particle Size Rating
Protozoa Giardia, Cryptosporidium 5 microns or larger Water filter 1.0–4.0 microns
Bacteria Cholera, E. coli, Salmonella 0.2–0.5 microns Microfilter 0.2–1.0 microns
Viruses Hepatitis A, rotavirus, Norwalk virus 0.004 microns Water purifier to 0.004 microns
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100
m~1
mm
Micro/Nanofluidic Desalination Method
V +pressure
V
V
nano-junction
seawater
brine
fresh water (50% recovery)
ANY chargedspecies
ion depletionboundary
Nature Nanotechnology, 2010, 5, 297.US provisional patent, TLO case # 12601 / 13218,
Fresh waterreservoir
500m
Brine reservoir
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Applied electric field (V/cm)
50 60 70 80
Con
duct
ivity
(mS/
cm)
0
10
20
30
40
50
Conductivity of Desalted Stream
Seawater (from Crane Beach, Ipswitch, MA)
Salt evenlydistributed
Partially desalted
Completely desalted atlow channel
~500 mM
~4 mM
drinkable water: <10 mM
Calculated power consumption ~ 3.5 Wh/L c.f.) RO ~ 5.0 Wh/L, ED ~ 20.0 Wh/L
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Removal Capability
1Å 1nm 10nm 100nm 1m 10m 100m
solutes,particles
ions
hormones
proteins
viruses
bacteria
clay particles
E. coli
DNA
hair
RBC WBC
atomic/ionic
lowmolecular
highmolecular
microparticle
macroparticle
separationprocess
electro-dialysiselectro-dialysis
reverseosmosisreverseosmosis
nanofiltrationnanofiltration
ultrafiltration
microfiltrationmicrofiltration
scale
micro/nanofluidic desalination / purification
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1,600 unit deviceson a 8’ diameter plate
Portable, Self-Powered System
~100W solar panel
With the massive parallelization, we can expect Total flow rate ~ 300mL/min (can supply 7 peoples’ basic need by 1hr) 3.5Wh/L can be supplied by photovoltaic cell (25mW/cm2) or battery (~70W)
Cost estimation of manufacturing 1 stack ~$500 including materials and machine fees, excluding labor and software
Massachusetts Institute of Technology Research Laboratory of Electronics
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Competition Cost: ICP vs. RO
Energy Costs
Maintenance Costs
Investment Costs
Tota
l cos
ts o
f RO
for c
onsu
mer
60k
Cos
t (U
SD
)
50k
40k
30k
20k
10k
5k
0.9 22 30 47 63 72 95 110 142 157 253
Water production rate (liter/hour)
ICP system production and setup costs per device
100 wafers / month500 wafers / month
Courtesy by iTeam project member at MIT
Massachusetts Institute of Technology Research Laboratory of Electronics
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Where can it be applied for?
Phase I, (2yrs) Phase II, (1yr)
ICP desalination
Individual use Community use
• Cost-insensitive application
• Flow rate ~ 100mL/min
• Should be easy of use
• High energy efficiency
• Large ships
• Rural areas
• Island communities
• Cost-sensitive application
• Flow rate ~ 1L/min
• Should be easy of use• High energy efficiency
• Shipboard application
• Disaster relief
• Recreational purpose
• Military / humanitarian use
Phase III, (2yrs)
Large-volume Apps
• Large scale desal plants based on ICP desalination
• Pre-treatment for large-scale existing desal plants
• Rare metal mining from seawater / groundwater
• Cost-sensitive application
• Flow rate >> 1L/min
• Should be easy of use• High energy efficiency