oxidative processes in water technology: intro€¦ · · 2014-07-14oxidative processes in water...
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Oxidative Processes in WaterTechnology:
Intro
Faculty of ChemistryChair of Instrumental Analytical Chemistry
Prof. Dr. Torsten C. Schmidt
• Diploma, Chemistry, 1994PhD, Analytical Chemistry, 1997(+ law studies 1994-1997)
• Postdoc Environmental Chemistry1998-2002
• Group Leader Environmental Chemistry and Analysis2002-2006
• Chair of Instrumental Analytical Chemistry since 2006 Director of the Center for Water and Environmental Research since 2009
• Scientific Director for WaterChemistry, IWW Water Centre since 2006
• President of the Water Chemical Society since 2013
http://www.uni-duisburg-essen.de/iac
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Dr. Jochen Türk• Diploma, Chemistry,
Technical University Dortmund, 2001
• PhD, Analytical ChemistryUniversity Duisburg – Essen, 2007
• Institute of Energy and Environmental Technology (IUTA), Duisburg since 2001 (Affiliated Institute of the University Duisburg-Essen) Head of Laboratory, Department of Environmental
Hygiene & Analysis, 2003 – 2008 Head of Department Research Analysis, since 2009
Analytical Technologies Waste water technologies Pharmaceuticals and micro pollutants
in the environmentContact: [email protected]
http://www.iuta.de
4Dr. Holger Lutze
Contact: [email protected]
• B.Sc. Water ScienceUniversity Duisburg-EssenThesis: Ozonation of benzotriazoles
Eawag aquatic research (Switzerland)(2005)
• M.Sc. Water ScienceUniversity Duisburg-Essen
Thesis: Degradation of taste and odor compounds in ozone based oxidationEawag aquatic research (Switzerland)(2007)
• Scientific assistant and advisorIWW Water Centre Feasibility studies on oxidants in water treatment Co-supervisior in different water treatment pilot studies(since 2008)
• Ph.D. on sulfate radical based oxidationUniversity Duisburg-Essen (funded by the Water Chemistry Society) Cooperation with IWW water center in several drinking water projects(since 2009/2010)
5Your Assistants: Sarah Willach
Since 2013 Ph.D. Instrumental Analytical Chemistry University Duisburg-Essen
Ph.D. Thesis Development of a liquid chromatography-15N-isotope ratio mass spectrometer interface
2010 – 2012 M.Sc. in Water ScienceUniversity Duisburg-Essen
Master Thesis(2012)
Optimisation and application of an analytical method for the determination of adsorbable organofluorinecompounds (AOF) in the water cycleTechnologiezentrum Wasser, Karlsruhe, Germany
2007 – 2010 B.Sc. in Water ScienceUniversity Duisburg-Essen
Bachelor Thesis(2010)
Effect of the pH on formation of disinfection by-products in swimming pool watersDanmarks Tekniske Universitet, Lyngby, Denmark
Ph.D. Student - University Duisburg-Essen - Germany
Contact: [email protected]
6Your Assistants: Alaa Salma
Since 2011 Ph.D. Instrumental Analytical Chemistry University Duisburg-Essen
Ph.D. Thesis Pharmaceuticals wastewater treatment by advanced oxidation processesInstitute of Energy and Environmental Technololgy, Duisburg
2004 – 2006 M.Sc. in Industrial Systems Safety and Environment ManagementDamascus University, Syria & Poitier University, France
Master Thesis(2006)
Analyses and Assessment of Hazard in York Unit for the Production of Ammonia Nitrogen Fertilizer plant & Damascus University, Syria
1999 – 2004 B.Sc. in Chemical SciencesDamascus University, Faculty of Science, Syria
Bachelor Thesis(2004)
Separation and Determination of Aromatic Hydrocarbons in KeroseneDamascus university, Faculty of science, Syria
Ph.D. Student - University Duisburg-Essen - Germany
Contact: [email protected]
Fields of Research: (Advanced) Oxidation Processes
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50
0 50 100 150 200 250
[Ozone] / µM
[Dic
lofe
nac]
and
[Pro
duct
s] /
µM
N
O
Cl
Cl
CH2
COOH
CH2N
CO2HH Cl
Cl
Current Research Projects: Development, Set-Up and Characterization of Nonthermal Plasmas by Corona
Discharge in Water Treatment (Svetlana Gasanova MC-ITN, Klaus Kerpen) Reactive Species in the Fenton Process (Alexandra Fischbacher, Alexandra Beermann) Sulfate Radicals in Oxidative Water Treatment (Holger Lutze) Behaviour of Complexing Agents in Oxidative Water Treatment with Focus on Gd
Complexes used in MRI (Maike Cyris) UV assisted Oxidation for Removal of Micropollutants in Wastewater (Alaa Salma) Mechanistic Aspects of the Reaction of Primary and Secondary Amines with
Ozone in Aqueous Systems (Agnes Tekle-Röttering external at Westfälische Hochschule)
Recent Funding
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Why do We Offer a Dedicated Courseon Oxidative Processes?
1. The use of oxidative processes is a common and important tool in watertreatment
2. Current political pressure for furtherremoval of micropollutants will increasedemand for advanced treatment optionsincluding AOPs
3. Oxidative processes play a major role in natural transformation processes
9The Mülheim Process for Treating
Ruhr River Water
Slow sandfiltration
Activated Carbon Filters
UV disinfection
Chlorine dosage
Chloro-dioxide dosage
NaOH dosage
Pre-Ozonation
If needed
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Ozonation in Wastewater Treatment
Conventional WWTP Ozone contactor Posttreatment River
Example: WWTP Bad Sassendorf (Lippeverband)
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Aims of the Lecture
• Overview of routine and state-of-the-art oxidative processes used in water and wastewater treatmentSmall overlap with the optional courses on water and wastewater treatment but hardly focus on technical implementation
• Advanced understanding of fundamental transformation processes involved in technical processes
• Evaluation of advantages and drawbacks of oxidative processes for exemplary applications
• Development of criteria for the selection of appropriate technological solutions
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Required Background
• Physical Chemistry: Thermodynamics, chemical equilibrium, mass balance equations, kinetics
• Organic Chemistry: Functional groups, Reaction mechanisms (including radical-based mechanisms)
• Water Chemistry: – Ions in aqueous solution (Acid/base, Dissolution, Complexation)– Redox chemistry – Homogenous transformation reactions– Photochemistry
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Organisation• Lecture and Tutorial
Wednesday 1415-1600, T03 R03 D89, Wednesday 1615-1700, T03 R03 D89
• Formation of groups for problem discussion and presentation • During the four tutorials up to May 21 each group presents their
solution to a specified problem in a problem set distributed in the course. Their approach will be discussed. It is NOT the primary goal to show the correct result but to learn how to tackle such problems. Group formation will be done by the PhD students after collecting contact data to ensure a good mixture of external/internal and German/international students.
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Organisation II2nd half of term:
Review Preparation and PresentationSubmission of a review on a distributed paper with emphasis on weaknesses, missing data etc. Short presentations of major findings during last two-three tutorials
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Course ContentsSubject Who? Date Date
TutorialIntroduction to oxidative processes and course organization
TS/All 09.04.14
Kinetic constants and oxidant exposure HL 16.04.14Ozone-based reactions HL 23.04.14 30.04.14Hydroxyl radical-based reactions HL 30.04.14 07.05.14Further oxidants HL 07.05.14 14.05.14Applications in water treatment (including disinfection) I
TS 14.05.14 21.05.14
Applications in water treatment (including disinfection) II
TS 21.05.14
Applications in wastewater treatment I JT 04.06.14Applications in wastewater treatment II JT 11.06.14 (11.06.14)Disinfection/transformation by-products: (Eco)toxicological evaluation
JT 18.06.14 18.06.14
Economical considerations JT 25.06.14 25.06.14Wrap-Up all 02.07.14Exam 23.07.14
or14.10.14
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Literature• Urs von Gunten, Clemens von Sonntag:
Chemistry of Ozone in Water and Wastewater Treatment: From Basic Principles to Applications.IWA Publishing, 2012
• Christiane Gottschalk, Judy Ann Libra, Adrian Saupe:Ozonation of Water and Waste Water: A Practical Guide toUnderstanding Ozone and its Applications. Wiley-VCH, 2009
• Thomas Oppenländer: Photochemical Purification of Water and Air: Advanced Oxidation Processes (AOPs): Principles, Reaction Mechanisms, ReactorConcepts. Wiley-VCH, 2002
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Are Oxidative Processes New Treatment Technologies?
Ozone Treatment Waterworks Hermannstadt1915
UV-Treatment 1915
Modified after M. Exner, U Bonn
Use of Oxidation Processes in Water Treatment
Advantages: • Constant process performance• Combined disinfection and pollutant control• No disposal of concentrates or solids
(compared with AC sorption or membrane filtration)
Areas of Use:• Drinking water
– Disinfection, Decolorization, Fe(II) andMn(II) Removal, Micropollutant Elimination, Taste and odor elimination
• Municipal wastewater– Disinfection, Further elimination of micropollutants
• Industrial wastewater• High purity industrial process waters
Common Oxidants in Water TreatmentOxidant Purpose
Direct addition to water
Oxygen/air Fe(II) oxidation
Chlorine (HOCl) Disinfection only (German DWG)
Chlorine dioxide Disinfection only (German DWG)
Ozone Disinfection/oxidation (also •OH)
Hydrogen Peroxide Oxidation (mainly •OH)
Permanganate Oxidation
Persulfate Oxidation (•OH and SO4•- )
In situ formation
OH radicals Oxidation/AOPs
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Important Considerations in Oxidative Treatment Processes
Pollutants Oxidation CO2, H2O LifetimeMechanismsKinetics
Transformation products
Biodegradability Toxicologicaleffects
Scavenging by matrix components
Possible lossof efficiency, Oxidation byproducts
Structuredeterminesreactivity, lesspronounced forOH
Oxidation
Modified after U. von Gunten, eawag
Energy Demand/Carbon Footprint?
Formation ofsecondaryoxidants
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Estrogen Receptor
Effect?Effect
Oxidation
Estrogenically active compound
Effect of Oxidative Transformation I:Reduction of Estrogenicity
Transformation product
binds?binds
Modified after U. von Gunten, eawag
17-Estradiole (E2)
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Reduction of estrogenicity is proportional to concentration decline of EE2
Lee et al. 2008
Reduction of Estrogenic Effects (EEEQ) of 17-Ethinylestradiole by Oxidative Processes
d o s e , M0 5 1 0 1 5 20 2 5 3 0
Rel
ativ
e EE
2 or
EEE
Q
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
R e la tiv e E E 20.0 0 .2 0 .4 0 .6 0 .8 1 .0
Rel
ativ
e EE
EQ
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0C h lo rin e
d o s e , M0 5 1 0 1 5 20 2 5 3 0
B ro m in e
R e la tiv e E E 20.0 0 .2 0 .4 0 .6 0 .8 1 .0
Rel
ativ
e EE
EQ
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
d o s e , M0 5 1 0 1 5 2 0 2 5 3 0
O zo n e
R e la tive E E 20 .0 0 .2 0 .4 0 .6 0 .8 1 .0
Rel
ativ
e EE
EQ
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
U V flu e n c e , m J /c m 20 1 00 2 0 0 3 00 4 0 0
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
O H ra d ic a l
R e la tiv e E E 20 .0 0 .2 0 .4 0 .6 0 .8 1 .0
Rel
ativ
e EE
EQ
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
d o s e , M0 5 10 1 5 2 0 25 30
C h lo rin e d io x id e
R e la tive E E 20.0 0 .2 0 .4 0 .6 0 .8 1 .0
Rel
ativ
e EE
EQ
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
d o s e , M0 10 2 0 3 0 40
F e rra te
R e la tive E E 20.0 0 .2 0 .4 0 .6 0 .8 1 .0
Rel
ativ
e EE
EQ
0 .0
0 .2
0 .4
0 .6
0 .8
1 .0
1
r2 = 0 .9 6 r2 = 0 .9 9
1 1
r2 = 0 .9 9
1
r2 = 0 .99
1
r2 = 0 .9 9
1
r2 = 0 .99
Rel
ativ
e EE
2 or
EEE
Q
EE2EEEQ
Modified after U. von Gunten, eawag17-Ethinylestradiole (EE2)
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Effect of Oxidative Transformation II:Reduction of Toxic Effects in Bulk Samples
• Data from WWTP Regensdorf, CH:
Adapted from S. Zimmermann, EPFL
Elimination by ozonation and slow sand filtration in %
Bioluminescence suppression
Acetylcholinesterase suppression
Algae test (photosynthesis)
Algae test (growth)
YES Assay
Describing Pollutant Removal
Oxidant nNo. of publ. kinetic const. kn (ca. 2008)
Ozone ~ 500OH Radicals ~ 2000Chlorine ~ 300
Chlorodioxide ~ 100
Ferrate(VI) ~ 50
1
n
n n
d Pk ox P
dt
10
lnn
n n
Pk ox dt
P
pH, T!
Quantification oxidant exposure:• Matrix dependent
• Dosage dependent
• Consideration of secondary oxidants
Determination kinetic constants:• Direct measurements
• Indirect measurements (Competition kinetics)
• Quantitative structure activity relationships
(QSARs)
• Estimation from similar oxidants
Modified after U. von Gunten, eawag
Oxidation kinetics: Estimation of Rate ConstantsQSAR for the Reaction of Phenols and Phenolates with
Ozone
o,m,p+
-1.5 -1.0 -0.5 0.0 0.5 1.0 1.5
log(
k O3)
2
4
6
8
10
Neutral speciesAnionic species
= -3.4(±0.3)y0 = 3.4(±0.1)r2 = 0.94
= -2.4(±0.2)y0 = 8.9(±0.1)r2 = 0.96
2-Cla
4-ClaPhOHa
triclosan
Penta-Cla
Penta-Brb
4-NO2a
2-OHb4-OHb
4-CH3a
3-CH3a
2-CH3a
2,6-CH3c
2,4-CH3c
3,4-CH3c
2,3-CH3c
4-Cla
triclosan2-Cla
PhOHa
O3O3O
Cl
ClCl
OH
O3
pKa = 8.1
Phenolates
Phenols
Triclosan
Modified after U. von Gunten, eawag
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0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0 50 100 150 200 250
norm
aliz
ed o
xida
nt-c
once
ntra
tion
Stability of Oxidants in Lake Zurich Water
Permanganate
Chlorine
Ferrate
Chlorine dioxideOzone
Time - min
Stability of oxidants: .OH (s) << O3 < ClO2 < HFeO4
- < HOCl < MnO4-
Modified after U. von Gunten, eawag
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Overview Advanced Oxidation ProcessesUV based Ozone based H2O2 based
UV/H2O2
UV/O3
O3/H2O2
No Chemicals
O3/AC
Ozonation
Fenton Ultrasound
UV/TiO2
H2O+Ultrasound OH +H
H2O + VUV(120-160nm) OH +H
2O3 + HO2- 2OH +3O2
O3 + AC OH + O2
O3 + (OH-, NOM) OH
H2O2 + UVC 2 OH (
O3+UVC H2O2 OH+O2
TiO2 + h h+ + e- OH + O2-
Vacuum UV (VUV)
OH- yield: 50%
[Fischbacher et al., ES&T 2013]
H2O2
Fe(II) Fe(III)
OH
H2O2HO2
[Fe(III)HO2]2+
Also directphotolysis
pH < 4
28Comparison of Advanced Oxidative Processes
UV based Ozone based H2O2 basedUV/H2O2(TiO2)
UV/O3
O3/H2O2
No Addition
Carbazon
Ozonation
FentonUltrasound
Energy demand
Vacuum UV
Loss of oxidation efficiency via matrix scavenging, assimilable organic carbon formation, unknown transformation products
Negative Effects
Modified after H. Lutze
BrO3-
NDMA
29Comparison of Advanced Oxidative Processes
UV based Ozone based H2O2 basedUV/H2O2(TiO2)
UV/O3
O3/H2O2
No Addition
Carbazon
Ozonation
FentonUltrasound
Energy demand
Vacuum UV
Loss of oxidation efficiency via matrix scavenging, assimilable organic carbon formation, unknown transformation products
Negative Effects
Modified after H. Lutze
Br- HOBr/OBr-
BrO3-
O3
O3/•OH
H2O2
Br-
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Introductory Words on ReactionMechanisms
• Oxidation processes: Transformation processes initiated by oxidants
• Reaction mechanisms:– Seldomly Electron transfer– Much more common since oxidants are electrophilic
reagents:• Addition to electron rich positions in organic molecules
(activated aromatics, olefines, deprotonated amines, reduced sulphur moieties)
• H-Abstraction (in particular OH radicals)• Substitution (in particular chlorine/HOCl)
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Efficiency of Oxidation Processes
• Decisive: Reaction rate of oxidant with target compound– Depending on electronic and structural properties of oxidant and
compound
• Lifetime of oxidant in water– Selectivity vs. unspecific reactivity– Matrix scavenging – Oxidant exposition (c x t)– Formation of oxidation byproducts
• Energy demand for specific removal rates
Modified after U. von Gunten, eawag