2.500 desalination and water purification...20 cm diam by 1 m length. source. this image and many of...
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MIT OpenCourseWarehttp://ocw.mit.edu
2.500 Desalination and Water Purification Spring 2009
For information about citing these materials or our Terms of Use, visit: http://ocw.mit.edu/terms.
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2.500 Desalination & Water Purification
Slides to accompany reverse osmosis discussion
3 March 2009Professor John H. Lienhard V
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Spiral-wound element
20 cm diam by 1 m length
Source. This image and many of the subsequent images are from:
M. Wilf and M. Balaban, Membrane Desalination and Membrane Filtration, L’Aquila, Italy: European Desalination Society, 2007.
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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3Source: Leon Awerbuch, desalination lecture at MIT, 23 Feb 2009
Courtesy of Leon Awerbuch. Used with permission.
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4Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Vertical centrifugal pumps & Membrane pressure vessels5
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Recovery per element is limited to about 18% to prevent excessive concentration polarization
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Concentrate may be staged in order to achieve high recovery without excessive concentration polarization, e.g., in brackish water RO (BWRO)
9Rp,1 stage ≲ 60% Rp,2 stage ≲ 75-85%
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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First stage has 32 pressure vessels; second stage has 14 10Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Concentrate staging in a high-salinity brackish RO system with 80% recovery. Note turbine assisted booster pump.
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Location
Flow, m3/h(gpm)Pressure,bar (psi)
TDS ppm 5881 5881 16313 16313 28444 139 657 240 28444
(7)0.5
(458)104.2
987654321
521.3 521.3 184.9 184.9 104.2(458) (1478) (355) (1833)
80.7 416.7336.0
20.823.214.217.1(248) (206) (336) (302)
(2294) (2294) (814) (814)
9 5
43
12 6 8
7
Rp=80%
Rp2=44%
Rp1=64%
Figure by MIT OpenCourseWare.
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High Pressure
Low Pressure
Pumping power = (Volume flow rate) * (pressure rise)The high pressure concentrate accounts for a large part of the pumping power
High Pressure
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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13Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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(Cyprus)14Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration.
L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Pelton Wheel 15
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Turbine impeller
Pump impeller
Shaft bearing
Energy recovery device
16Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Turbocharger applied as interstage booster pump 17
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Permeate blending in a low-salinity brackish RO system with 89% recovery
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1 2
3
4
5
6
7
TDS, ppm
Pressure, bar (psi)
Flow, m3/h(gpm)
647
657.4 490.6 166.8 490.6 73.5 416.7 583.5
647
8 3.3(116) (48)
647 647 4107 41 215
(2893) (2159) (734) (2159) (323) (1833) (2567)
Location 1 2 3 4 5 6 7
Rp=89%
Rp1=85%
Figure by MIT OpenCourseWare.
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Permeate may be blended to lower feed salinity in SWRO
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TDS, ppm
Pressure, bar (psi)
Flow, m3/h(gpm)
45199
979.0 992.2 992.2 575.5 138.9 138.9 13.9
44695
62.8 10.7(911)
64.4(934) (155)
7.1(103)
44695 76707 977 977 9153 68 245 190
(4308) (2159) (4369) (2534) (611) (611) (61)125(550)
277.8(1222)
402.8(1772)
Location 1 2 3 4 5 6 7 8 9 10
1 2 3
4
5 6
8
10
7
9
Figure by MIT OpenCourseWare.
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Source: R.H. Stewart, OceanWorld website, TAMU.
Ocean surface temperatures in July and January
20Courtesy of Robert H. Stewart. Used with permission.
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Correction for temperature change
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Temperature correction factor (representative):
TCF = exp[-2700(1/T-1/298)] for T in kelvin.
Both A and B in solution-diffusion model are multiplied by the TCF.
TFC = 1 at T=298 K. TCF rises with increasing temperature.
Membrane permeability (for both water and salt) rises with temperature: P = P0 exp(-E/RT)
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(at fixed flux)
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Feedwater preheating can be beneficial, especially if supply is relatively cold.
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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This 10,000 gpd (38 m3/day) system costs ~$40K. With ancillary hardware, it is ~$60K, plus site preparation and related costs.
A 100,000 gpd (380 m3/day) system is ~$600K, with ancillary systems.
Typical applications include Caribbean resorts and hotels.
Image removed due to copyright restrictions. Please see http://www.tsgwater.com/images/specs_10k.pdf
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Representative Seawater RO Intake
Hydrostatic feed
Intake 10 to 15 m below surface at low tide.
25Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Seawater pretreatment.
Disinfect with chlorine
Add ferric chloride to coagulate small particulates
Filter, adjust pH to protect membranes, add scale inhibitor
dechlorination (by sodium bisulfate), cartridge filtration (5-15 μm porosity) 26
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Cartridge filter housing in a horizontal configuration 27
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Seawater RO Post-treatment.
Add alkalinity and hardness via: CO2+Ca(OH) → Ca(HCO3)2
Disinfect with additional chlorine, control pH 29
Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration. L'Aquila, Italy: European Desalination Society, 2007. Used with permission.
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Diffuser for concentrate discharge
Effluent volume: 67,000 m3/dDischarging velocity: 6.0 m/sConcentrated seawater: 5.8%Raw seawater: 3.5%
Distance (m)
Concentration (%)30 Figures from: Wilf, M., and M. Balaban. Membrane Desalination and Membrane Filtration.
L'Aquila, Italy: European Desalination Society, 2007. Used with permission.