A Portable and Battery-Powered Seawater Desalination

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A Portable and Battery-Powered Seawater Desalination
A Portable and Battery-Powered
Seawater Desalination Device by
Ion Concentration Polarization
Dr. Sung Jae Kim,
Prof. Jongyoon Han
November 16, 2010
Micro/Nanofluidic BioMEMS Group,
Department of Electrical Engineering and Computer Science,
Massachusetts Institute of Technology
Research Laboratory of Electronics
Water Resource on the Earth
ILP
R&D
World Water Development Report
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2/12
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Global Water Market
ILP
R&D
Market volume
2007 (USD bn)
Expected annual
growth
Sewage treatment
104
4%
Equipment for wastewater treatment
12
6%
Chemicals and services for the industry
13
4%
Membrane systems for wastewater treatment
4.2
19%
Drinking water purification
129
4%
(Sales of bottled water)
(91)
(10%)
Ozone treatment
0.3
10%
UV treatment
0.5
14%
Treatment using membrane systems
1.9
20%
Thermal desalination plants
2.5
4%
Desalination plants with membrane
2.4
8%
Desalination plants running operation
7.3
9%
Wastewater
Drinking water
Desalination
Source: Global water Intelligence: Global Water Market 2008
Massachusetts Institute of Technology
3/12
Research Laboratory of Electronics
Fresh Water in Resource-Limited Setting
ILP
R&D
2.6 billion people do not use improved sanitation
Brackish ground water
Disaster-stricken areas
Groundwater turns brackish
Disaster relief, military and
humanitarian operation
www.sacbee.com
www.who.int
Underdeveloped area
Lack of delivery and on-grid
infrastructures
Worldwide use of improved sanitation
facilities in 2008
www.un.org
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4/12
WHO report 2010
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Conventional Seawater Desalination
Reverse Osmosis
• Best energy efficiency ~ 5 Wh/L
• Requires large scale plants and
significant membrane fouling
www.watertechnology.net
Electro-Dialysis
• Less membrane fouling
• Worse energy efficient ~ 20 Wh/L
www.thewatertreatments.com
Thermal distillation / freezing
• Easiest method
• Energetically costly
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5/12
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ILP
R&D
Competing Technologies
ILP
R&D
Small/Medium scale desalination / purification system
• Household RO machine with UV lamps only for tap water like groundwater
e.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-efficient
e.g. Ampac Seapro 100 (>$7650), 30-90Wh/L
• Other technologies focusing on particulate/organics, not salt
e.g. spiral filtration system (PARC)
chemical agent for inducing flocculation-sedimentation
activated 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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6/12
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Micro/Nanofluidic Desalination Method
ILP
R&D
500m
Brine reservoir
100m~1mm
ne
i
r
b
ANY charged
V+
species
pressure
seawater
V
fresh water (50% recovery)
V
ion depletion
boundary
Fresh water
reservoir
nanojunction
Nature Nanotechnology, 2010, 5, 297.
US provisional patent,
TLO case # 12601 / 13218,
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Conductivity of Desalted Stream
ILP
R&D
Seawater (from Crane Beach, Ipswitch, MA)
50
~500 mM
Conductivity (mS/cm)
40
30
Completely
desalted at
low channel
20
Salt evenly
distributed
Partially desalted
10
~4 mM
0
50
60
70
80
drinkable water: <10 mM
Applied electric field (V/cm)
Calculated power consumption ~ 3.5 Wh/L
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c.f.) RO ~ 5.0 Wh/L, ED ~ 20.0 Wh/L
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Removal Capability
1Å
scale
1nm
atomic/
ionic
solutes, ions
particles
10nm
low
molecular
100nm
high
molecular
proteins
10m
micro
particle
bacteria
100m
macro
particle
hair
E. coli
DNA
hormones
reverse
osmosis
separation
process
1m
ILP
R&D
viruses
clay particles
RBC
WBC
nanofiltration
ultrafiltration
electrodialysis
microfiltration
micro/nanofluidic desalination / purification
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Portable, Self-Powered System
1,600 unit devices
on a 8’ diameter plate
~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
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ILP
R&D
Competition Cost: ICP vs. RO
ILP
R&D
60k
Energy Costs
30k
20k
ICP system production and
setup costs per device
100 wafers / month
500 wafers / month
Maintenance Costs
for consumer
40k
Total costs of RO
Cost (USD)
50k
10k
Investment Costs
5k
0.9
22
30
47
63
72
95
110
142
157
253
Water production rate (liter/hour)
Courtesy by iTeam project member at MIT
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11/12
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Where can it be applied for?
ICP desalination
Phase I, (2yrs)
Phase II, (1yr)
Individual use
Community use
• Shipboard application
• Large ships
• Disaster relief
• Rural areas
• Recreational purpose
• Island communities
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
• Military / humanitarian use
• Flow rate ~ 100mL/min
• Flow rate ~ 1L/min
• Flow rate >> 1L/min
• Cost-insensitive application
• Cost-sensitive application
• Cost-sensitive application
• Should be easy of use
• Should be easy of use
• Should be easy of use
• High energy efficiency
• High energy efficiency
• High energy efficiency
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12/12
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ILP
R&D
ILP
R&D
“One tiny gap in a channel,
One giant leap for better life”
Questions?
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13/12
greenhelm.spyestate.com
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