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Nitrification and the Removal of Micropollutants from Wastewater. AzSGC. SpaceGrant Mentor Dr. Robert Arnold Chemical and Environmental Engineering University of Arizona. SpaceGrant Intern Dave Newman Civil Engineering University of Arizona. Arizona SpaceGrant Consortium - PowerPoint PPT Presentation
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Nitrification and the Removal ofMicropollutants from Wastewater
Arizona SpaceGrant ConsortiumUndergraduate Research Internship Program Symposium
April 18, 2008
SpaceGrant MentorDr. Robert Arnold
Chemical and Environmental EngineeringUniversity of Arizona
SpaceGrant InternDave NewmanCivil Engineering
University of Arizona
AzSGC
Endocrine Disrupting Chemicals (EDCs)AzSGC
• Chemicals that mimic or block hormones and disrupt normal functions
• Concentrations in environment are generally in the 1 to 100 parts per trillion range (ng/L)
• Structural commonalities include aromatic rings and large size
• Ecological effects include gonadal egg development and skewed sex ratios
EDC MW[g/mol]
Solubility[mg/L ]
Log KOW
E2 Relative Potency
Description
Estrone (E1) 270.4 13.0 3.43 0.38 Estrogen metabolite
17-Estradiol (E2) 272.4 13.0 3.94 1.0 Primary estrogen in vertebrates
Estriol (E3) 288.4 13.0 2.81 0.024 Estrogen metabolite
Ethinyl Estradiol (EE2) 296.4 4.8 4.15 1.19 Oral contraceptive ingredient
Nonylphenol (NP) 220.0 5.4 4.48 0.00014 Surfactant, detergent
Kidd et al 2007Estrone Ethinyl EstradiolEstriol17-Estradiol
Nonylphenol
Measured Concentrations for 30 FrequentlyDetected Organic Wastewater Contaminants AzSGC
Kolpin et al 2002
= Known Estrogenic Effects
Micropollutants in the Environment
AP/CNN 03/10/08
Kolpin et al 2002
AzSGC
EDCs in Wastewater Treatment
• Wastewater represents ongoing point source as well as centralized treatment opportunity
• AC, MBR, ozonation, UV radiation, ultra filtration and advanced oxidation have, at times, indicated high removal efficiencies
• However, most common treatment process in US is Activated Sludge (AS)
• Nitrifying AS systems have indicated increased removal efficiency over non-nitrifying AS systems
• Required US infrastructure improvements/upgrades estimated in hundreds of billions
• Jones et al 2007 estimated advanced treatment strategies 1.5 to 2.5 times more expensive than conventional AS
Clara et al 2004
Nitrification >10 days
AzSGC
Study Objectives and Design
Objectives• Establish a bench-scale, completely-mixed AS reactor
• Operate reactor over nitrifying and non-nitrifying conditions
• Dose influent with nonylphenol and investigate treatment performance
AzSGC
Clarified Effluent ClarifierSynthetic WastewaterCMAS ReactorBioStat MD Control Unit
Pumpsp-Nonylphenol
“Between the Idea and the Reality…Lies the Shadow” (T.S. Elliot)
The Research ProcessAzSGC
• Equipment Refrigerator, Pumps, BioStat, Glass, Piping
• Reactor Parameters and WW Recipe V = 1 L, = 6 hr, Q = 4 L/d Synthetic WW (Esperanza et al 2004)
• AS Seeding and Pilot Testing Inoculated w/ sludge from Ina Road BNR Train Operate system hydraulically
• Issues and Hurdles Hydraulic and Mechanical
Field ResultsAzSGC
• Ina Road Water Pollution Control Facility Activated Sludge 2 Treatment Trains (Nitrifying and Non-Nitrifying)
• Measured Estrogenic Activity using in vitro Bioassay
Courtesy of Bingfeng Dong, Ph.D. Student, UA, CHEE
Future WorkAzSGC
• Batch Reactor “Proof of Concept” Investigate nitrification via Ion Chromatograph 200 mL batch reactor, seeded with CMAS sludge Dose with nonylphenol (NP) Allow to operate for 5 days Measure NP using GC-ECD
• Run CMAS as continuous flow
• Operate over range of sludge ages
• Dose with other EDCs?
AcknowledgementsAzSGC
Dr. Bob Arnold, SpaceGrant MentorDr. Eduardo Saez
Brian BarbarisBingfeng Dong & Alandra Kahl
Susan BrewMatt Giardina & AzSGC Staff
Sondra TeskeJeff and Mario
Arla AllenCharley Amling & UA Glass Shop
Questions or Comments?AzSGC