Date post: | 13-Jan-2017 |
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Removal of pharmaceuticals in different
activated sludge wastewater treatment
plants in comparison to biofilm and
ozonation
1
Kai Bester, Aarhus University
VERSITET
Micro-pollutants in activated sludge treatment
Inflow Sludge treatment effluent
sludge
Partition
ing
Deg
ra-
dat
ion
Metabolites?
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
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
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
First order reaction rate constants WWTP Compounds Degradation rate k Half-Life R2
% h-1 [h-1]
Aalborg West
Naproxen 90 0.0196 15 0.85
Ketoprofen 90 0.0079 36 0.79
Fenoprofen 90 0.0407 7 0.90
Carbamazepine - - - -
Triclosan 85 0.0065 44 0.97
Dichlofenac - - - -
Aalborg East
Naproxen 46 0.0026 86 0.67
Ketoprofen 77 0.0082 27 0.85
Fenoprofen 55 0.0088 25 0.92
Carbamazepine 82 - 70 0.45
Triclosan 61 0.0022 100 0.94
Dichlofenac - - - -
Aalbybro
Naproxen 62 0.0278 6 0.77
Ketoprofen 78 0.0112 14 0.77
Fenoprofen 65 0.0087 18 0.84
Carbamazepine - - - -
Triclosan 85 0.0038 40 0.97
Dichlofenac - - - -
Hirtshals
Naproxen 90 0.0132 13 0.91
Ketoprofen 94 0.0125 14 0.96
Fenoprofen 90 0.0813 2 0.83
Carbamazepine - - - -
Triclosan 91 0.0044 40 0.98
Dichlofenac - - - -
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
Degradation of Fenoprofen in in sludge from four different WWTPs (AAL : Aalborg).
-3.00
-2.50
-2.00
-1.50
-1.00
-0.50
0.00
0.50
0 5 10 15 20 25 30 35
Ln(
C/C
0)
Time (hours)
Hirtshals AAL East Aabybro AALWest
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
Degradation rate k in dependence of biomass expressed as volatile solids (VS).
0
0.01
0.02
0.03
0.04
2 3 4 5
De
grad
atio
n R
ate
K (
h-1
)
Volatile Solids (g/L)
Naproxen
Ketoprofen
Fenoprofen
Triclosan
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
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
De
grad
atio
n R
ate
K (
h-1
)
Sludge Retention Time (days)
Naproxen
Ketoprofen
Fenoprofen
Triclosan
Chen, Vollertsen, Lund Nielsen, Gieraltowska Dall, Bester, Ecotoxicology, 24, 2073–2080, 2015
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?
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
Single stage denitrifying MBBR
0.0
0.2
0.4
0.6
0.8
1.0
Rela
tive c
on
cen
trati
on
Sulfamethoxazole
Sulfamethizole
Trimethoprim
0.2
0.4
0.6
0.8
1.0
0.0
0.2
0.4
0.6
0.8
1.0
Sta
rt e
xper
imen
t
Time (d)
Rela
tive c
on
cen
trati
on
0.2
0.4
0.6
0.8
1.0
Atenolol
Metoprolol
Sotalol
Propranolol
Sta
rt e
xper
imen
t
Time (d)
0.0
0.2
0.4
0.6
0.8
1.0
0
50
100
150
200
250
MeOH-fed MBBR
Ss depleted
Rela
tive c
on
cen
trati
on
0
50
100
150
200
250Erythromycin
Clarithromycin
sCOD
SS
EtOH-fed MBBR
Ss depleted
mg
CO
D L
-1
0.0
0.2
0.4
0.6
0.8
1.0R
ela
tive c
on
cen
trati
on
Citalopram
Venlafaxine
Carbamazepine
0.0
0.2
0.4
0.6
0.8
1.0
Rela
tive c
on
cen
trati
on
Iomeprol
Iohexol
Diatrizoic acidIopamidol
Iopromide
0.0
0.5
1.0
1.5
Rela
tive c
on
cen
trati
on
Acetyl-Sulfadiazine
Sulfadiazine
a
b
c
d
e
f
Torresi, Escola Casas, Polesel, Plósz, Christensson, Bester 2016, Water Research, in press
0.0
0.2
0.4
0.6
0.8
1.0
Rela
tive c
on
cen
trati
on
Sulfamethoxazole
Sulfamethizole
Trimethoprim
0.2
0.4
0.6
0.8
1.0
0.0
0.2
0.4
0.6
0.8
1.0
Sta
rt e
xper
imen
t
Time (d)
Rela
tive c
on
cen
trati
on
0.2
0.4
0.6
0.8
1.0
Atenolol
Metoprolol
Sotalol
Propranolol
Sta
rt e
xper
imen
t
Time (d)
0.0
0.2
0.4
0.6
0.8
1.0
0
50
100
150
200
250
MeOH-fed MBBR
Ss depleted
Rela
tive c
on
cen
trati
on
0
50
100
150
200
250Erythromycin
Clarithromycin
sCOD
SS
EtOH-fed MBBR
Ss depleted
mg
CO
D L
-1
0.0
0.2
0.4
0.6
0.8
1.0
Rela
tive c
on
cen
trati
on
Citalopram
Venlafaxine
Carbamazepine
0.0
0.2
0.4
0.6
0.8
1.0
Rela
tive c
on
cen
trati
on
Iomeprol
Iohexol
Diatrizoic acidIopamidol
Iopromide
0.0
0.5
1.0
1.5
Rela
tive c
on
cen
trati
on
Acetyl-Sulfadiazine
Sulfadiazine
a
b
c
d
e
f
Single stage denitrifying MBBR
• Denitrifying MBBR is nearly as effective as aerobic
• MeOH reactor does a bit better than the EtOH reactor
• Diclofenac cannot be degraded under denitrifying conditions
• Carbamazepine and X-ray contrast compounds can be degraded under denitrifying conditions
Torresi, Escola Casas, Polesel, Plósz, Christensson, Bester 2016, Water Research, in press
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
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