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Science and Technology for Sustainable Water Supply

Published byDrake Jaggars Modified over 4 years ago


Presentation on theme: "Science and Technology for Sustainable Water Supply"— Presentation transcript:

1 Science and Technology for Sustainable Water Supply
Menachem Elimelech Department of Chemical Engineering Environmental Engineering Program Yale University Thank you for the kind introduction. My talk will be on the “Science and Technology for Sustainable Water Supply”, a subject which has a great societal impact, and in which engineering can play a very important role. “Your Drinking Water: Challenges and Solutions for the 21st Century”, Yale University, April 21, 2009

2 The “Top 10” Global Challenges for the New Millennium
Energy Water Food Environment Poverty Terrorism and War Disease Education Democracy Population It is not surprising that water and energy are on the top of this list. In fact, as you will see later in my talk, water and energy are interrelated. Several of the other top challenges are also indirectly related to water and energy. Richard E. Smalley, Nobel Laureate, Chemistry, 1996, MRS Bulletin, June 2005

3 1) 25% of world population, 33% of developing world population – will live in areas of water scarcity 2) Areas shown as not water scarce will need to greatly increase their fresh water productivity (catchment, distribution, etc) 3) Areas shown as not water scarce have regional scarcity International Water Management Institute

4 Regional and Temporal Water Scarcity
We need to look at regional and temporal water scarcity – not average for the entire country. The IPCC report tells us that dry areas getting drier, wet areas wetter, flow more seasonal (less storage in snow and ice). Improved catchment and redistribution are needed, but these will have environmental impacts (such as those of dams on river systems and fisheries), and can be energy intensive. National Oceanic and Atmospheric Administration

5 How Do We Increase the Amount of Water Available to People?
Water conservation, repair of infrastructure, and improved catchment and distribution systems ― improve use, not increasing supply! Increase water supplies to gain new waters can only be achieved by: Reuse of wastewater Desalination of brackish and sea waters

6 Many Opportunities We are far from the thermodynamic limits for separating unwanted species from water Traditional methods are chemically and energetically intensive, relatively expensive, and not suitable for most of the world New systems based on nanotechnology can dramatically alter the energy/water nexus We are far from the thermodynamic limits for separating unwanted species from water. This will be analyzed in our discussion on desalination where thermodynamics dictates the minimum theoretical energy to desalinate a saline solution. 6

7 Co-authored a review paper with colleagues in the Center for Advanced Materials for Purification of Water with Systems. The paper discusses a few of the issues addressed in my presentation.

8 Wastewater Reuse

9 Reclaimed Wastewater in Singapore (NEWater)
Source of water supply for commercial and industrial sectors (10% of water demand) 4 NEWater plants supplying 50 mgd of NEWater. Will meet 15% of water demand by 2011 To give an example of a successful implementation of relaimed water, I am citing the example of NEWater. NEWater is produced from the reclamation of treated used water. It is now a reliable source of water supply for the commercial and industrial sectors, accounting for about 10% of Singapore’s water demand. Currently there are four NEWater plants supplying 50mgd of NEWater. From the figure, you can see the locations of the 4 NEWater plants and the pipeline system supplying reclaimed water to the industrial and commercial areas for direct non-potable usage and to the reservoirs for indirect potable usage. The long-term target is to meet 15% of our water demand through NEWater by the year 2011. 5 miles

10 Reuse of Wastewater in Orange County, California
Groundwater Replenishment System, GWR (70 MG/day)) Prado Dam Santa Ana River Facilities Another example is the Groundwater Replenishment System in Orange County, California. This is a major upgrade of Water Factory 21 that was completed in 1975. Treated wastewater is used to recharge groundwater in Orange county, that later used for drinking water. This is a classic example of wastewater reclamation for indirect potable use.

11 GWR System for Advanced Water Purification (Orange County)
Microfiltration (MF) Reverse Osmosis (RO) Ultraviolet Light with H2O2 OCSD Secondary WW Effluent Recharge Basins The treatment scheme of the GWR system – which is considered nowadays as state-of-the-art. MF (pretreatment)RO  oxidation/disinfection

12 Namibia, Africa

13 Natural Beauty … but not Enough Water

14 Windhoek’s Solution: Wastewater Reclamation for Direct Potable Use
Goreangab Reclamation Plant (Windhoek) “Water should not be judged by its history, but by its quality.” Dr. Lucas Van Vuuren National Institute of Water Research, South Africa The only wastewater reclamation plant in the world for direct potable use

15 The Treatment Scheme: A Multiple Barrier Approach

16 Most Important: Public Acceptance and Trust in the Quality of Water
Breaking down the psychological barrier (the “yuck factor”) is not trivial Rigorous monitoring of water quality after every process step Final product water is thoroughly analyzed (data made available to public) The citizens of Windhoek have a genuine pride in the reality that their city leads the world in direct water reclamation

17 Wastewater Reuse: Membrane Bioreactor (MBR)-RO System
Future wastewater reuse will use MBR Skip MF/UF used in the previous scheme Less energy/cost, smaller footprint Shannon, Bohn, Elimelech, Georgiadis, and Mayes, Nature 452 (2008)

18 Fouling Resistant UF Membranes: Comb (PAN-g-PEO) Additives
amphiphilic copolymer added to casting solution segregate & self-organize at membrane surfaces PEO brush layer on surface and inside pores Doctor Blade Coagulation Bath Casting Solution Heat Treatment Bath Casting Solution Doctor Blade Coagulation B ath Heat Treatment For successful and cost/energy effective operation of MBR and wastewater reuse we need membranes with low fouling propensity. In this study, polyacrylonitrile-graftpoly(ethylene oxide) (PAN-g-PEO), an amphiphilic comb copolymer with a water-insoluble polyacrylonitrile (PAN) backbone and hydrophilic poly(ethylene oxide) (PEO) side chains, was used as an additive in the manufacture of novel PAN UF membranes. During casting, the PAN-g-PEO additive segregates to form a PEO brush layer on all membrane surfaces, including internal pores. Fouling Resistance Asatekin, Kang, Elimelech, Mayes, Journal of Membrane Science, 298 (2007)

19 Fouling Reversibility (with Organic Matter)
White: Pure water Gray: recovered flux after fouling/cleaning (following “physical” cleaning (rinsing) with no chemicals) Wettability, pure water permeability, and resistance to irreversible fouling increased when either the amount of PAN-g-PEO added to the membrane or the PEO content of the comb copolymer was increased. In this the PEO content of the comb copolymer was fixed (50%) In 24-h dead-end filtration studies, blend membranes prepared with 20 wt% PAN-g-PEO (comb PEO content: 39 wt%) were found to resist irreversible fouling by 1000 ppm solutions of bovine serum albumin (BSA), sodium alginate, and humic acid, recovering the initial pure water flux completely by a pure water rinse, or a backwash in the case of humic acid. Shannon, Bohn, Elimelech, Georgiadis, and Mayes, Nature 452 (2008)

20 AFM as a Tool to Optimize Copolymer for Fouling Resistance
Kang, Asatekin, Mayes, Elimelech, Journal of Membrane Science, 296 (2007)

21 Wastewater Reuse: Membrane Bioreactor (MBR)-RO System
Shannon, Bohn, Elimelech, Georgiadis, and Mayes, Nature 452 (2008)

22 One Step NF-MBR System? NF

23 Antifouling NF Membranes for MBR (PVDF-g-POEM)
Filtration of activated sludge from MBR PVDF-g-POEM NF: no flux loss over 16 h filtration PVDF base: 55% irreversible flux loss after 4 h Commercial polyvinylidene fluoride (PVDF) UF membranes were coated with the amphiphilic graft copolymer poly(vinylidene fluoride)-graft-poly(oxyethylene) methacrylate, PVDF-g-POEM, to create thin film composite (TFC) nanofiltration membranes. The PVDF UF base membrane served as the control in filtration experiments Activated sludge from aerobic MBR. Tests at 40 psi for coated, 10 psi for base. Pure water permeabilities up to 56 L/m2 hMPa were obtained at pressures of 0.21MPa (30 psi). The new TFC NF membranes exhibited no irreversible fouling in 10-day dead-end filtration studies of model organic foulants bovine serum albumin, sodium alginate and humic acid at concentrations of 1000 mg/L and above. Dead-end filtration of activated sludge from an MBR (1750 mg/L volatile suspended solids, VSS) resulted in constant flux throughout the 16 h filtration period. Fouling performance of the TFC NF membrane and effluent water quality were substantially improved in all cases over that for the base PVDF UF membrane. PVDF-g-POEM (●,●) PVDF base (,) Asatekin, Menniti, Kang, Elimelech, Morgenroth, Mayes: J. Membr. Sci. 285 (2006) 81-89

24 Wastewater Reuse: Osmotically-Driven Membrane Processes

25 Wastewater Reclamation with Forward (Direct) Osmosis
Concentrate Disposal

26 Osmotic MBR-RO: Low Fouling, Multiple Barrier Treatment
OMBR SYSTEM DISINFECTION Wastewater Potable water Sludge RO Achilli, Cath, Marchand, and Childress, Desalination, 2009.

27 Reversible Fouling: No Need for Chemical Cleaning
Mi and Elimelech, in preparation.

28 Desalination: Reverse Osmosis

29 Population Density Near Coasts




33 Seawater Desalination
Augmenting and diversifying water supply Reverse osmosis and thermal desalination (MSF and MED) are the current desalination technologies Energy intensive (cost and environmental impact) Reverse osmosis is currently the leading technology

34 Reverse Osmosis Major improvements in the past 10 years
Further improvements are likely to be incremental Recovery limited to ~ 50%: Brine discharge (environmental concerns) Increased cost of pre-treatment Use prime (electric) energy (~ 2.5 kWh per cubic meter of product water)

35 Minimum Energy of Desalination
Minimum energy needed to desalt water is independent of the technology or mechanism of desalination Minimum theoretical energy for desalination: 0% recovery: 0.7 kWh/m3 50% recovery: 1 kWh/m3

36 Nanotechnology May Result in Breakthrough Technologies
“These nanotubes are so beautiful that they must be useful for something. . .”, Richard Smalley ( ).

37 Aligned Nanotubes as High Flux Membranes for Desalination?
Hinds et al, “Aligned multi-walled carbon nanotube membranes”, Science, 303, 2004.

38 Research on Nanotube Based Membranes
Mauter and Elimelech, Environ. Sci. Technol., 42 (16), , 2008.

39 Next Generation Nanotube Membranes
Mauter and Elimelech, Environ. Sci. Technol., 42 (16), , 2008. Single-walled carbon nanotubes (SWNTs) with a pore size of ~ 0.5 nm are critical for salt rejection Higher nanotube density and purity Large scale production?

40 Bio-inspired High Flux Membranes for Desalination
Natural aquaporin proteins extracted from living organisms can be incorporated into a lipid bilayer membrane or a synthetic polymer matrix

41 BUT …. Energy is Needed Even for Membranes with Infinite Permeability
Minimum theoretical energy for desalination at 50% recovery: 1 kWh/m3 Practical limitations: No less than 1.5 kWh/m3 Achievable goal:  2 kWh/m3 Shannon, Bohn, Elimelech, Georgiadis, and Mayes, Nature 452 (2008)

42 Desalination: Forward Osmosis

43 The Ammonia-Carbon Dioxide Forward Osmosis Desalination Process
Nature, 452, (2008) 260 Energy Input McCutcheon, McGinnis, and Elimelech, Desalination, 174 (2005) 1-11.

44 NH3/CO2 Draw Solution NH3(g) CO2(g) NH3(g) CO2(g) HEAT NH4HCO3(aq)
(NH4)2CO3(aq) NH4COONH2(aq) HEAT

45 High Water Recovery with FO
RO FO 1 2 3 4 5 6 7 8 9  (atm) R e c o v r y ( % ) Seawater  Explain recovery Recovery is the ratio of the freshwater volume recovered to the total feed volume RO recovery is often lower

46 Energy Use by Desalination Technologies (Equivalent Work)
Contribution from Electrical Power McGinnis and Elimelech, Desalination, 207 (2007)

47 Waste Heat Geothermal Power

48 Concluding Remarks We are far from the thermodynamic limits for separating unwanted species from water Nanotechnology and new materials can significantly advance water purification technologies Advancing the science of water purification can aid in the development of robust, cost-effective technologies appropriate for different regions of the world

49 Acknowledgments

Download ppt "Science and Technology for Sustainable Water Supply"
 Seawater Desalination: Energy and Technology Department of Chemical and Environmental Engineering Yale University USA Menachem Elimelech Sharing Knowledge. Integrating Water Management The Future of Integrated Water Management: Moving the Program Forward Gary Bardini, Deputy Director CA Department of Water. Wastewater Management at an Animal Protein Rendering Facility J.B. Hess, W.A. Dozier, J. Spann and B. Thomas Poultry Science Department, Auburn University. Scott Reinert , P.E. Water Resources Manager El Paso Water Utilities Decentralised Wastewater Management Treatment of Waste Brine from a Brackish Reverse Osmosis Plant By Clark C.K. Liu, Ph.D., P.E., F. ASCE Professor Emeritus of Civil and Environmental Engineering, University of Hawaii Former Director for Environmental. The Energy – Water Nexus : UT School of Law. Brackish vs Seawater. SPI – “The Membrane Technology Consultants” James C. Vickers, P.E. Vice President Separation Processes, Inc Lionshead Ave. Suite 2 Carlsbad, CA Industrial Wastewater Treatment and Zero Liquid Discharge 1 Wastewater and Water Re-Use in Israel Eng. Alexander Kushnir Director General Israel Water & Sewage Authority March 2012. AQUAREC Project Centre for Water Systems AQUAREC Project Centre for Water Systems D. Joksimovic. Team Sludge Team 17: Jon Reimink, Ernie Sarkipato, Josh Terpstra, Ryan Voogt. Drinking Water Through Recycling The benefits and costs of supplying direct to the distribution system Dr Stuart Khan School of Civil & Environmental Engineering,