Kai Bester - Aarhus University, Denmark - Removal of pharmaceuticals in different activated sludge wastewater treatment plants in comparison to biofilm and ozonation
Presentation at the ESPP workshop Pharmaceuticals in sewage biosolids, Malmo, 27-10-2016
European Sustainable Phosphorus Platform (ESPP)
www.phosphorusplatform.eu
Sustainable management of nutrients is crucial for agriculture, food, industry, water and the environment. ESPP brings together companies and stakeholders to address the Phosphorus Challenge and its opportunities for the circular economy.
Countries:
Austria AT
Belgium BE
Bulgaria BG
Cyprus CY
Czech Republic CZ
Germany DE
Denmark DK
Estonia EE
Spain ES
Finland FI
France FR
Greece EL
Hungary HU
Ireland IE
Italy IT
Lithuania LT
Luxembourg LU
Latvia LV
Malta MT
Netherlands NL
Poland PL
Portugal PT
Romania RO
Sweden SE
Slovenia SI
Slovakia SK
United Kingdom UK
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Phosphorus:
Fosfor
Fosfor
Fòsfòr
Фосфор
Fosfor
Фосфор
Fosfor
Fosfor
Фосфор
Фосфор
Fosforas
Fosfors
Fuosfuors
Fosfor
Ffуsfforws
Fosfar
Fosfaras
Fosfaar
Fosforus
Φωσφορος
Ֆոսֆոր
Fosfor
Fosfor
Фосфор
Фосфор
ফসফরাস
فسفر
ફૉસ્ફરસનો
फास्फोरस
Fosfor
Fosfori
Foszfor
Фосфор
Фосфор
Паликандур
Fosfor
Fosfor
Фосфор
Фосфор
Фосфор
Фосфор
Fosfor
فوسفور
Fosfor
Fosforoa
ფოსფორი
[fūsfūr]
זרחן
Fosfru
Lìn
リン
인
ฟอสฟอรัส
Photpho
磷
Posporo
Fosfor
Pūtūtae-whetū
Fosforus
ഫോസ്ഫറസ്
பொஸ்பரசு
Fosofo
Fosforase
Posfori
Fósforo
Phusphuru
Fosforimi
Fosforo
Fosforon
Pesticium
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Kai Bester - Aarhus University, Denmark - Removal of pharmaceuticals in different activated sludge wastewater treatment plants in comparison to biofilm and ozonation
1. Removal of pharmaceuticals in different
activated sludge wastewater treatment
plants in comparison to biofilm and
ozonation
1
Kai Bester, Aarhus University
VERSITET
3. Micro-pollutants in activated sludge treatment II
Typically 10 g/L sludge are generated
If lg partition constant is 3: 50% of
compound is in sludge
If lg partition constant is 4: 90% of
compound is in sludge
lg partition constant = pKow
6. Systematic comparison of different sludges
• Sludges were sampled at the respective WWTP
• They were used in lab for incubation studies under
normalised aerobic conditions
• Samples were taken and analysed for
pharmaceuticals – for kinetic data
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
7. WWTPs used:
Name PE COD
/
BOD
Temp
[oC]
SRT
[d]
HRT
[h]
VS
[g/L]
N P
Aalborg-
West
300.000 2.7 12 14 22 2.45 Alternating
DN in
aeration
Biological-
sidestream
hydrol.
Aalborg-
East
100.000 2.9 11 31 35 3.17 Alternating
DN in
aeration
Biological-
sidestream
hydrol.
Aabybro 11.000 2.1 11 47 21 4.51 Upstream DN FeSO4
Hirtshals 62.700 2.0 7 20 42 3.93 Alternating
DN in
aeration
Biological-
upstream hydrol.
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
11. Degradation rate k as a function of sludge retention
time (SRT).
0
0.01
0.02
0.03
0.04
0 10 20 30 40 50
DegradationRateK(h-1)
Sludge Retention Time (days)
Naproxen
Ketoprofen
Fenoprofen
Triclosan
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
12. Status on sludge
• Classical activated sludge can degrade some compounds
• It is difficult to predict which plant will be able to remove
how well.
• Some compounds cannot be removed (Diclofenac,
Carbamazepine, X-ray contrast media)
• Diclofenac and Carbamazepine can be removed with
polishing ozonation, while X-ray contrast media cannot
• Ozonation is energy craving
• What can be achieved with biofilms?
15. Staged aerobic MBBR
• 21/26 compounds
degraded >20%
• First order kinetics
for most compounds
• Two phase kinetics
for four compounds
• While M1 degrades
faster, has M3
usually the more
effective biomass
Escola Casas, Chhetri, Ooi, Hansen, Litty, Christensson, Kragelund, Andersen, Bester, Water Research, 83, 293-302, 2015
Including removal for Diclofenac, Carbamazepine, X-ray contrast compounds
16. Single stage denitrifying MBBR
0.0
0.2
0.4
0.6
0.8
1.0
Relativeconcentration
Sulfamethoxazole
Sulfamethizole
Trimethoprim
0.0
0.2
0.4
0.6
0.8
1.0
0
50
100
150
200
250
MeOH-fed MBBR
Ss depleted
Relativeconcentration
0
50
100
150
200
250
Erythromycin
Clarithromycin
sCOD
SS
EtOH-fed MBBR
Ss depleted
mgCODL-1
0.0
0.2
0.4
0.6
0.8
1.0
Relativeconcentration
Citalopram
Venlafaxine
Carbamazepine
0.0
0.5
1.0
1.5
Relativeconcentration
Acetyl-Sulfadiazine
Sulfadiazine
a
b
c
d
Torresi, Escola Casas, Polesel, Plósz,
Christensson, Bester 2016, Water
Research, in press
18. Conclusions:
• MBBRs might be a suitable alternative for removing
organic micro-pollutants
• Co-degradation and starvation are most probably the
most relevant process.
• Currently residence times of 20 h would be needed to
break down sufficient amounts of pollutants
• It is difficult to foresee reactor parameters for fully
optimised co-degradation/starvation reactors
19. Acknowledgement
All the students and collaborators that helped moving these themes forward:
Xijuan Chen, Monica Escola Casas, Haitham El-taliawy, Gordon Ooi, Kai Tang,
Elena Torresi
Founding: MST, MUDP, DFF-FTP, AUFF, Havs och Vatten Myndigheden
Collaboration partners: AAU, DTU, ANOX Kaldnes, Kruger, TI, Aarhus Vand,
Herning Vand, Biofos
20. 20
CAS Ozonation Biofilm
X-ray contrast
media
Beta-blockers
Diclofenac/
Carbamazepine
?
Ibuprofen
Sulfonamides :-/
Macrocyclic
antibiotics
?
Persistence of compound groups in
wastewater treatment