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Transcript of Wastewater
Municipal and Domestic
Wastewater Treatment
TheThe Largest Biotechnology Largest Biotechnology Industry in the World …Industry in the World …
……and the least understood?and the least understood?
Veolia Water N° 1 worldwide for water services; revenue of €12.5 billion for 2008; providing drinking water and wastewater treatment services to more than 139 million people around the world; 93,433 employees; Permanent operations in 64 countries; Managing close to 4,400 contracts around the world.
•62,000 employees serving •68 million people worldwide with drinking water •44 million people for wastewater services •46 million people for waste collection service •Revenues of $18.4 billion in 2007 •An R&D budget of $95 million for water research
Wastewater is the biggest waste by volume Wastewater is the biggest waste by volume in New Zealand. Approximately 1.5 billion in New Zealand. Approximately 1.5 billion litres of domestic wastewater is discharged litres of domestic wastewater is discharged into the environment daily. into the environment daily.
Wastewater in Auckland:
Watercare wastewater from about 800,000 people wastewater from about 800,000 people industrial customers equivalent of 370,000 people. industrial customers equivalent of 370,000 people. 290,000 cubic metres of wastewater each day.290,000 cubic metres of wastewater each day.
North Shore City WTP serves 199,000 peopleNorth Shore City WTP serves 199,000 people
Other plants in Pukekoe,Waiuku, Beachlands, Kumeu, Other plants in Pukekoe,Waiuku, Beachlands, Kumeu, Orewa, Warkworth, Helensville, Waiheke Cleavdon, Orewa, Warkworth, Helensville, Waiheke Cleavdon,
on site treatment all rural propertieson site treatment all rural properties
What is wastewater? (aka Sewage)
Water (99%)Water (99%) OrganicsOrganics NutrientsNutrients Toxic materialsToxic materials Infectious agentsInfectious agents Plus??Plus??
http://www.earthwise.dep.state.pa.us/content/knowledgedocs/pdf/WastewaterCompositionComparisons.pdf
Faecal coliform Bacteria (MPN/100ml x106)50 60 100
Copper (mg/l) 0.14 0.17 0.21Chromium 0.003 0.01 0.016Cadmium 0.04 0.08 0.16Nickel 0.01 0.06 0.11Lead 0.05 0.1 0.2Zinc 0.19 0.29 0.38
Henry and Heinke 1989 Environmental science and engineering, Prentice Hall p416
Waste product for treatment and disposal?
or
Resource to recover and use?
Discussion
What should waste treatment achieve?What should waste treatment achieve? What are the microbiological processes that What are the microbiological processes that
can be coopted?can be coopted? Control strategies to optimise the microbial Control strategies to optimise the microbial
function.function.
Wastewater treatment
What should waste What should waste treatment achieve?treatment achieve?
Recover Materials and Recover Materials and EnergyEnergy
Remove or Reduce Remove or Reduce Environmental and Human Environmental and Human Health Risk Health Risk
Priorities for reduce or Priorities for reduce or removeremove
Safely Dispose of ResidueSafely Dispose of Residue
Wastewater treatment
Faecal coliform Bacteria (MPN/100ml x106)50 60 100
Copper (mg/l) 0.14 0.17 0.21Chromium 0.003 0.01 0.016Cadmium 0.04 0.08 0.16Nickel 0.01 0.06 0.11Lead 0.05 0.1 0.2Zinc 0.19 0.29 0.38
What are the microbiological processes that can be coopted?
Biodegradation - Biodegradation - BioconversionBioconversion Removal/separation Removal/separation
– flocculation – flocculation attachment to attachment to surfacessurfaces
Inactivation, lysis Inactivation, lysis Faecal coliform Bacteria (MPN/100ml x106)50 60 100
Copper (mg/l) 0.14 0.17 0.21Chromium 0.003 0.01 0.016Cadmium 0.04 0.08 0.16Nickel 0.01 0.06 0.11Lead 0.05 0.1 0.2Zinc 0.19 0.29 0.38
Microbial Processes and Influences Biodegradation
biomass + energy+ residual Biodegradation requires degrading organisms and supporting assemblage
(enzymes and cofactors) Amenable contaminant - physical and chemical state contact between MO and contaminant environment - Temp, pH, Oxygen, Nutrients limiting substances, ionic strength. relative proportions of components
BioconversionBioconversion Removal Removal InactivationInactivation
Microbial Processes and Influences
BiodegradationBiodegradation BioconversionBioconversion
Incomplete biodegradationIncomplete biodegradation degrading organisms and supporting assemblage
• (enzymes and cofactors) Amenable contaminant - physical and chemical state contact between MO and contaminant environment - Temp, pH, Oxygen, Nutrients limiting substances, ionic strength. relative proportions of components
Removal Removal InactivationInactivation
Microbial Processes and Influences
BiodegradationBiodegradation BioconversionBioconversion
Removal Removal adsorption, attachment, incorporation and adsorption, attachment, incorporation and
deposition or separation (specific or non-deposition or separation (specific or non-specific)specific)
InactivationInactivation Degradation, starvation, stress, Degradation, starvation, stress,
Biological wastewater treatment and processes directed at biological components Eg Eg Activated sludgeActivated sludge Fixed growth reactorFixed growth reactor Suspended media reactorSuspended media reactor Aerated ditchAerated ditch Oxidation pondOxidation pond Constructed wetlandConstructed wetland Anaerobic digestionAnaerobic digestion
Eg disinfectionEg disinfection Oxidation pondsOxidation ponds
Typical treatment train
Settlement
Biological treatment
Clarification
Disinfection
Discharge
Inflow
Remove solids and fats
Reduce carbon and nutrients
Remove biological solids
Reduce pathogens
Mangere Wastewater Treatment Plant current
Screening Earth Filter
clarification
Activated sludge
Sludge
Primary Settling
CH4 gas Anaerobic Digester
DewateringLandfillEffluent
Discharge
Disinfection: Anthracite filter and UV
odor
Mangere Wastewater treatment plant:
Activated sludge Reactors/Clarifier
Activated sludge Reactors/Clarifier Objective:
Reduce solids, BOD, COD, Nitrogen, fats and oils in liquid flow
Mechanism: Enhancement of microbial activity to induce floc
formation and settlement and remove contaminants to sludge
biodegradation POC+ DOC+N Biomass
Sorption of other contaminant eg metals, HC Stirring and aeration
Microbiological players bacteria community dominated by facultative
organotrophic bacteria. eg Pseudomonas, Flavobacterium Achromobacter,
Micrococcus, Bacillus, Acinetobacter Filementous bacteria eg Nocardia, Zooglea, Thiothrix,
Nostocoida, Microthrix, Sphearotilus yeasts and moulds to a lesser extent Protozoa, rotifers. worms
Extracellular polymer linkers forming flocs of settlable Extracellular polymer linkers forming flocs of settlable densitydensity
Sludge treatment – biogas production
Nitrogen removal
Why remove nitrogen?Why remove nitrogen? Where does nitrogen come from?Where does nitrogen come from? What is the form of nitrogen in wastewater?What is the form of nitrogen in wastewater?
Classical N cycle
Ahn Y-H. Process Biochem 42 2006 p 1709 - 1721
Nitrogen removal N = approx 12% of cell mass N mostly removed -through cell removal Nitrification - chemoautotrophic bacteria
Slow growing 10 + days sludge age NH4
+ + 2O2 NO3- + 2H+ +H2O
Nitrosomonas, Arthrobacter, ? 3NH4
+ + 3O2 2NO2- + 4H+ +2H2O
Nitrobacter, Arthrobacter? 2NO2
- + O2 2NO3-
Denitrification – eg Pseudomonads, Thiobacillus denitrificans
C6H12O6 + 4NO3- 6CO2 + 6H2O + 2N2
NO3- NO2 - NO N2O N2
Anaerobic ammonium oxidation (anammox)
Ahn Y-H. Process Biochem 42 2006 p 1709 - 1721
Anammox
Anammox "anaerobic ammonium oxidation". Anammox "anaerobic ammonium oxidation". The anammox reaction is :The anammox reaction is :
NH4+ + NO2- = N2 + 2H2O + energyNH4+ + NO2- = N2 + 2H2O + energy This reaction is carried out by a group of This reaction is carried out by a group of
planctomycete bacteria. Two of those have been planctomycete bacteria. Two of those have been named provisionally: named provisionally: CandidatusCandidatus "Brocadia "Brocadia anammoxidans" and anammoxidans" and CandidatusCandidatus "Kuenenia "Kuenenia stuttgartiensis". stuttgartiensis".
http://www.anammox.com/research.http://www.anammox.com/research.
Nitrite reductase
Hydrizine hydrolase
Hydrazine dehydrogenase
http://www.anammox.com/anammox_mechanism.html
Last updated: March 9, 2004
Anommox Applicationhttp://www.anammox.com/application.html
wastewater streams high in ammonium (>0.2 g/l) and low wastewater streams high in ammonium (>0.2 g/l) and low in organic carbon (C:N ratio lower than 0.15). The two in organic carbon (C:N ratio lower than 0.15). The two processes proceed as follows:processes proceed as follows:
partial nitrificationpartial nitrification
2NH2NH44++ + 1.5O + 1.5O22=NH=NH44
++ + NO + NO22-- + H + H22O + 2HO + 2H++
anammoxanammox
NHNH44++ + NO + NO22
--=N=N22 + 2H + 2H22O O totaltotal
2NH2NH44++ + 1.5O + 1.5O22=N=N22 + 3H + 3H22O + 2HO + 2H++
Requires: 50% less oxygen. May reduce operational costs by Requires: 50% less oxygen. May reduce operational costs by 90%, 90%,
decrease in COdecrease in CO22 emissions of more than 100% emissions of more than 100%
Nitrosomonas aerobic denitrification
Ahn Y-H. Process Biochem 42 2006 p 1709 - 1721
Overall Nitrogen web
Ahn Y-H. Process Biochem 42 2006 p 1709 - 1721
What happens to Nitrogen at Mangere WTP
Assignment:Mangere Complex adds NZ$1b to Auckland City Economy. The just completed upgrade of the Mangere Materials Complex adds the final The just completed upgrade of the Mangere Materials Complex adds the final
process to allow complete recovery of the materials from what was once process to allow complete recovery of the materials from what was once called wastewater. The wastewater also called sewage was collected at the called wastewater. The wastewater also called sewage was collected at the plant and partly treated before being tipped into the Manukau harbour. The plant and partly treated before being tipped into the Manukau harbour. The cost of this treatment both in $ terms and in environmental cost was in excess cost of this treatment both in $ terms and in environmental cost was in excess on $50 m in 2010. Recovery of the resources that was once waste and the on $50 m in 2010. Recovery of the resources that was once waste and the industries linked to them are now worth over $1 b. industries linked to them are now worth over $1 b.
The most notable successes have been….The most notable successes have been….
NZ Herald May 12 2025NZ Herald May 12 2025
Assignment:Assignment: the to do.. Complete the next 10 paragraphs of the
Newspaper Article (5%) plus 2 page document in point form that
provides more information and some ideas on the approach to reclamation of resources (with references) (10%)
Due date: Monday May 31st Submit to SRC by 4 pm Value 15% of final mark
Field Visit : Wednesday 19 May Mangere Wastewater treatment plant Mangere Wastewater treatment plant Leave outside SBS at 11.00 am sharp Leave outside SBS at 11.00 am sharp Closed in shoes – no Sandals or JandalsClosed in shoes – no Sandals or Jandals Objectives Objectives
To understand the treatment processTo understand the treatment process To identify the strengths and weaknesses of the process and the To identify the strengths and weaknesses of the process and the
main constraints on treatment and disposal of wastemain constraints on treatment and disposal of waste Identify the pressures on the process to perform effectivelyIdentify the pressures on the process to perform effectively Identify areas where there is opportunity for improvement or Identify areas where there is opportunity for improvement or
benefit.benefit.
Own Transport?Own Transport?
Older reviews:Older reviews: Ahn Y-H Sustainable nitrogen elimination biotechnologies: A Review. Ahn Y-H Sustainable nitrogen elimination biotechnologies: A Review. Process Biochemistry 41, 2006, 1709 - 1721Process Biochemistry 41, 2006, 1709 - 1721 Mendoza-Espinosa, Leopoldo Stephenson, Tom. A review of biological aerated filters (BAFs) for wastewater Mendoza-Espinosa, Leopoldo Stephenson, Tom. A review of biological aerated filters (BAFs) for wastewater
treatment treatment Environmental Engineering Science. 16(3). 1999. 201-216.Environmental Engineering Science. 16(3). 1999. 201-216. Stratful, I.; Brett, S. Scrimshaw, M. B.; Lester, J. N.. Biological phosphorus removal, its role in phosphorus recycling Stratful, I.; Brett, S. Scrimshaw, M. B.; Lester, J. N.. Biological phosphorus removal, its role in phosphorus recycling
Environmental Technology. 20(7). July, 1999. 681-695.Environmental Technology. 20(7). July, 1999. 681-695. Grady, C. P. L., Jr. Filipe, C. D. M. . Ecological engineering of bioreactors for wastewater treatment Grady, C. P. L., Jr. Filipe, C. D. M. . Ecological engineering of bioreactors for wastewater treatment Water, Air, & Water, Air, &
Soil Pollution. 123(1-4). October, 2000. 117-132Soil Pollution. 123(1-4). October, 2000. 117-132 de-Bashan, Luz E.; Bashan, Yoav Recent advances in removing phosphorus from wastewater and its future use as de-Bashan, Luz E.; Bashan, Yoav Recent advances in removing phosphorus from wastewater and its future use as
fertilizer (1997-2003) fertilizer (1997-2003) Water Research. 38(19). November 2004. 4222-4246.Water Research. 38(19). November 2004. 4222-4246. Mallick, Nirupama. Biotechnological potential of immobilized algae for wastewater N, P and metal removal: A Mallick, Nirupama. Biotechnological potential of immobilized algae for wastewater N, P and metal removal: A
review. review. BioMetals. 15(4). December 2002. 377-390.BioMetals. 15(4). December 2002. 377-390. Low, Euan W.; Chase, Howard A.. Reducing production of excess biomass during wastewater treatment Low, Euan W.; Chase, Howard A.. Reducing production of excess biomass during wastewater treatment Water Water
Research. 33(5). April, 1999. 1119-1132.Research. 33(5). April, 1999. 1119-1132. Aksu, Zumriye. Application of biosorption for the removal of organic pollutants: A review Aksu, Zumriye. Application of biosorption for the removal of organic pollutants: A review Process Biochemistry. Process Biochemistry.
40(3-4). March 2005. 997-1026.40(3-4). March 2005. 997-1026. Lazarova, V. ; Savoye, P. Janex, M. L.; Blatchley, E. R., III Pommepuy, M. [Author]. Advanced wastewater Lazarova, V. ; Savoye, P. Janex, M. L.; Blatchley, E. R., III Pommepuy, M. [Author]. Advanced wastewater
disinfection technologies: State of the art and perspectives disinfection technologies: State of the art and perspectives Water Science & Technology. 40(4-5). Aug.-Sept., 1999. Water Science & Technology. 40(4-5). Aug.-Sept., 1999. 203-213.203-213.
Chuichulcherm, S.. An integrated system for the bioremediation of wastewater containing xenobiotics and toxic Chuichulcherm, S.. An integrated system for the bioremediation of wastewater containing xenobiotics and toxic metals metals Engineering in Life Sciences. 4(4). August 2004. 354-357.Engineering in Life Sciences. 4(4). August 2004. 354-357.
Books that contain helpful sections ( not on close reserve)Books that contain helpful sections ( not on close reserve) Fry et al : 1992 Microbial control of pollution: Society for General Microbiology. Fry et al : 1992 Microbial control of pollution: Society for General Microbiology. Gray NF 2004 :Biology of Gray NF 2004 :Biology of wastewaterwastewater treatment 2nd ed. Imperial College Press, London. treatment 2nd ed. Imperial College Press, London. Gerardi M and Zimmerman M :2004 Wastewater Pathogens: Electronic reproduction Somerset, New Jersey : Wiley Gerardi M and Zimmerman M :2004 Wastewater Pathogens: Electronic reproduction Somerset, New Jersey : Wiley
InterScience, [electronic resource] InterScience, [electronic resource]
Suggested Reading Ekama George A [a]; Wentzel Mark C [a]. Difficulties and developments in
biological nutrient removal technology and modelling. Water Science & Technology. 39(6). March, 1999. 1-11. ( try via science direct)
Fuerhacker M; Bauer H; Ellinger R; Sree U; Schmid H; Zibuschka F; Puxbaum H. Approach for a novel control strategy for simultaneous nitrification/denitrification in activated sludge reactors. Water Research. 34(9). June, 2000. 2499-2506
Strous Marc; Van Gerven Eric; Zheng Ping; Kuenen J Gijs; Jetten Mike S M [a]. Ammonium removal from concentrated waste streams with the anaerobic ammonium oxidation (Anammox) process in different reactor configurations. Water Research. 31(8). 1997. 1955-1962
Krumins Valdis; Hummerick Mary; Levine Lanfang; Strayer Richard; Adams Jennifer L; Bauer Jan. Effect of hydraulic retention time on inorganic nutrient recovery and biodegradable organics removal in a biofilm reactor treating plant biomass leachate. Bioresource Technology 85. December, 2002. 243-248.