city speak xii - water we drink: bevis mak of aecom
TRANSCRIPT
City Speak - The Water We Drink:
Water Treatment Technology and Demand Management
Bevis MakExecutive Director, Water, AECOM
15 May 2010
From Source to Tap – How Does It Work?
• A brief history of water treatment
• What is in our raw water?
• Treatment philosophy and method
• Sustainable water resources planning– Demand management– New water sources: Seawater– New water sources: Reuse
• Conclusion
Page 2
A Brief History of Water Treatment
Historical Development of Water Treatment (1)
• 1676: Microorganisms found under microscope
• 1746: First patent for a filter design. Commercial product in 1750 consisting sponge, charcoal and wool
Page 4
• 1804: First treatment plant in Scotland using filters
• 1854: first report case tracing a terrible epidemic of cholera due to contamination of water by a cholera victim recently returned from India
• 1931: Virus identified by electron microscope
Historical Development of Water Treatment (2)
• 1930s: With filtration and chlorination, no more waterborne disease outbreak in US
• 1950-80: Major improvements in cost effective treatment design:- clarification + filtration
• 1974: Chlorine + organics in raw water = trihalomethanes + other carcinogens (DBP disinfection by-products)
• 1993: Outbreak in Milwaukee identified a new organism: cryptosporidium and giardia (C&G) [54 deaths, 700+ ill; False alarm in Sydney in1998]
• 1990s: Advanced treatment technology - membranes, ozone and UV
Page 5
Giardia (4-14 micron)
Cryptosporidium (4 - 6 microns)
What is in our raw water?
Our Water
• Source water from rivers, lakes, groundwater reservoirs
• Many inorganic, organics and biological matters in raw water
• Inorganics : calcium, magnesium, sodium, potassium, carbonate, sulphate, chloride, nitrogen,
Page 7
phosphorus, iron, manganese etc
• Organics: mostly natural decomposition of plant and animal material, + synthetic (industrial and agricultural)
• Biological: bacteria, viruses, algae, other micro-organisms (protozoans such as C&G etc, helminths etc)
Particles in Water – How dirty does it look?
• Finely divided solids not generally distinguishable by the unaided eye
• Mainly from soil weathering processes and biological activities
• Potential absorption sink for toxic substances such as heavy metal and DBP
• Can cause strong scattering of incident light and leads to degradation of visibility
Page 8
• Clear water < 1NTU; runoff with sediment 40+ NTU
Treatment Philosophy and Method
World Health Organization (WHO) “Guidelines for Drinking-water Quality” 2006 (WHO 2006)
• … Securing the microbial safety of drinking-water supplies is based on the use of multiple barriers, from catchment to consumer, to prevent the contamination of drinking-water or to reduce contamination to levels not injurious to health. Safety is increased if multiple barriers are in place…
• Impounding reservoirs - self cleaning and dilution
• Treatment processes – minimum 2 processes, and each process enhances efficiency of next process
Page 10
Our Water Sources
• 30% local catchment water and 70%+ Dongjiang water
• Reservoirs:– Local catchment with excellent water quality: High Island, Shek Pik,
Tai Tam, Kowloon and Aberdeen Groups of Reservoirs– Local catchment with partial mixing by Dongjiang water: Tai Lam
Chung, Shing Mun Reservoirs– Main storage for Dongjiang water: Plover Cove Reservoir
• Most major treatment plants treats Dongjiang water direct, eg, Sha Tin Water Treatment Works handles 40% of supply daily
• Quality of Dongjiang water affects treatment options
Page 11
What Are the Key Concerns in Our Water?
• 5 most “difficult” parameters:– Avoid DBP formation (health) – oxidant / dosing point– Ammonia (health) – oxidation, biological– Manganese (aesthetics, brown water) - oxidation– Turbidity (health and aesthetics) – clarification + filtration– 4 log (99.99%) removal/reduction of C&G (health) – advanced
treatment needed
• What’s in Dongjiang water:
Page 12
Parameter Acceptable Historic High Max. Av.Ammonia 0.05 4.69 2.14 0.05
Manganese 0.05 1.25 0.72 0.05
Post 2003 at STWTW (in mg/L; ppm)
Conventional Treatment Approach
• Soluble organics / inorganics: chemical reaction to make them insoluble [Mn2+ → Mn4+ (MnO2)]
– Ozone if available (chlorination no long practiced)
• Insoluble particles – make them stick and bigger, carry with them the micro-organism and other toxic substance, and settle out faster – Addition of alum at pH 6.0-6.5 (polymer optional)
• After most organics are removed in above process, add chlorine for oxidation if needed to avoid formation of DBP
• Finer particles are removed by filtration
• Chlorine added for final disinfection
Page 13
The Process Diagram
Page 14
Before and After Clarification
Page 15
Solids formed after coagulation and flocculation
Traditional Clarifiers
Page 16
Filtration
Page 17
• Dual media
• Biofilters
Site Utilization – When Land Becomes An Issue
• Traditional clarifiers robust and stable
• Gravitation, with minimum energy
• But they are slow with large land intake
• Can they be more efficient?
Page 18
Clarification Process Foot Print
Conventional100%
Solids Contact - 40 %Superpulsator - 17%DAF - 14%DensaDeg - 10%Adsorption Clarifier - 6%Actiflo - 3%
• Proprietary systems are smaller, but are more energy and/or chemical intensive
• Long term O&M cost
C&G Treatment
• Mainly from human and animal waste pollution
• Can cause serious gastrointestinal problems to immuno-compromised population: 54 death and 700+ ill in Milwaukee 1993
• 4-log removal of C&G required for new WTW built after 2003
• Conventional treatment (clarification + filtration) inadequate: either by membrane (replacing clarification+filtration) or addition of ozone/UV disinfection
• Not a major problem for Hong Kong
Page 20
How’s Our Treated Water Like?
• Treated Water Quality Standards:– Primarily WHO Guidelines 2006– USEPA standards– EC standards
• WSD samples regularly:– 4 Microbiological parameters– 92 Chemicals of health significance– 15 other parameters
• Full compliance based on the annual average of monitoring data in accordance with international practice
Page 21
Sustainable Water Resource Planning
Sustainable Water Resources Planning Portfolio
Conservation Reuse
Desalination
Groundwater Surface Water
Brackish WaterSea Water
GeneralIndirect PotableDirect Potable
Sustainable Water Resource Planning
Demand Management
Water Demand Management – Conserve What We Have
• Education on water conservation: good practices on use of water and water savings
• Promotion on use of water saving devices
• Leakage control – pressure management and replacement of aging pipes
• Extension on use of sea water for toilet flushing
Page 25
Sustainable Water Resource Planning
New Water Source –Seawater Desalination
Seawater Desalination – Thermal Process
• Not quality or salinity dependent
• Multi-stage systems with heat recovery
• Much more efficient than the 1973 system but still significantly more expensive than membrane system; viable only co-locate with power plant
Page 27
Photo from: WSD “Water for a Barren Rock”
Completed 1976
Demolished 1992
Seawater Desalination – Thermal Process
Page 28
Al Hidd MED Plant, Bahrain (273 ML/d)
Seawater Desalination – Reverse Osmosis Membrane Process
• A membrane is like a paper filter, a physical barrier, but holes are much smaller, and is designed to take much higher pressure
• Latest material: Polyvinylidene Difluoride (PVDF)
• Pore size/ Pressure– Micro/ultra filtration (MF/UF)– Nanofiltration (NF)– Reverse osmosis (RO)
Page 29
4 to 6 micron0.1 micron pore size
0.0001 0.001 0.01 0.1 1 10 100mm
hairCrypto-sporidium
smallest micro-
organism
polio virus
Suspended solids
Parasites
Bacteria
Org. macro. molecules
Viruses
ColloidsDissolved salts
Sand filtration
Microfiltration
Ultrafiltration
Nanofiltration
Reverse Osmosis
Membrane Pore Size Smaller than Most Microorganisms
MF/UF: -0.2 to 2.0 bar (1 bar = 10m depth of water)NF: 5 to 9 barRO: 10 to 100 bar
Seawater Desalination
• All membrane units are VERY expensive; so is energy cost
• Many contaminants in seawater will cause fouling:
– Some contaminants can precipitate on the membrane surface
Page 31
– Microrganisms can grow on the membrane surface– Some chemicals can chemically degrade the membranes
• Must have good pre-treatment and screening: Normally MF/UF + RO
• RO cannot completely eliminate boron; second pass RO needed
Process Diagram
Page 32
Pilot Testing of Desalination in Hong Kong
• WSD conducted pilot testing of sea water desalination at Tuen Mun and Al Lei Chau
• At Tuen Mun – dilution from Pearl River but seasonal variations and organics increase bio-fouling
• At Ap Lei Chau – higher salinity but more consistent seawater quality
Page 33
Sustainable Water Resource Planning
New Water Source –Reclamation / Reuse
Water Reclamation / Reuse
• Treated secondary effluent is a major water source
• Technologically, easier to treat than seawater – more consistent quality
• Australia, California, Singapore – indirect potable or industrial use using MF/UF + RO, similar to seawater desalination
• Public acceptance is a major obstacle
Page 35
Water Reclamation / Reuse – Hong Kong Applications
• Ngong Ping: Sand filtration + UV after secondary treatment
• Shek Wu Hui STW Pilot Scheme: MF/UF + chlorine disinfection after secondary treatment
• Water used for irrigation, toilet flushing and water features
Page 36
Summary and Conclusion
Conclusion
• Technology has an important role to play in – providing a safe drinking water, and– Tapping into new water sources
• There is a price tag to new technology:– Higher capital cost of more expensive equipment– Higher energy and chemical cost because of higher level of
treatment– Higher maintenance cost because of expensive spares and
replacements– Higher carbon footprint
Page 38
To put the numbers into perspective: O&M Cost(Process +power / maintenance / staffing)
* high cost due to high membrane replacement cost against small production/demand]
There is a price to be paid!
Page 39
O&M Cost Power Only
Conventional $0.16/m3 $0.02/m3
Desalination (MF+RO) $4.0/m3 $1.8/m3
Reuse (MF+Cl2)* $5.2/m3 $0.8/m3
But …we do not wish to see this again!
Page 40
So, conserve now!
Thank You