Extensions of the Benchmark Simulation Model no2 with ... · Gürkan Sin . DTU Chemical...
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Extensions of the Benchmark Simulation Model no2 with processes for nitrous oxide and side-stream partial nitritation/Anammox treatment CAPEC-PROCESS Research Center Riccardo Boiocchi Krist V. Gernaey Gürkan Sin
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Outline • Extension of the BSM2 with N2O production processes (the BSM2N)
• Extension of the BSM2N with PN/A reactor (the BSM2NplusCANR)
• Uncertainty analysis of BSM2N predictions
• Sensitivity analysis of BSM2N predictions
• Comparison between the BSM2N and the BSM2NplusCANR
• Conclusions
• Future perspectives
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Introduction
3 21 July 2015
BENCHMARKING OF CONTROL STRATEGIES FOR HIGH EFFLUENT QUALITY, ENERGY SAVINGS,……
Not for BENCHMARKING OF CONTROL STRAGIES FOR N2O emission MINIMIZATION and ENHANCEMENT SIDE-STREAM N REMOVAL
ASM1
Inclusion of N2O production and stripping processes
2 EXTENSIONS:
Inclusion of a PN/A reactor in the side stream
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Extension of the Benchmark Simulation Model No2 with N2O dynamics- the BSM2N
4 21 July 2015
Activated Sludge Model for Greenhouse Gases no1 (ASMG1) by Guo and Vanrolleghem (2013)
N2O PRODUCTION PROCESSES (a) AUTOTROPHIC DENITRIFICATION
(b) HETEROTROPHIC DENITRIFICATION
N2O STRIPPING
ASM-to-ADM interface updated to include NO2
-, NO and N2O into the pool of electron acceptors used for organic carbon oxidation
Benchmark Simulation Model no2 for Nitrous oxide (BSM2N)
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Extensions of the Benchmark Simulation Model No2 with side-stream N removal - the BSM2NplusCANR
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Complete Autotrophic Nitrogen Removal model (CANRM)
ü AOB
x NOB
ü AnAOB ~ HB
by Vangsgaard et al. (2012)
NEW ASM- t o -CANRM INTERFACES developed
IMPLEMENTED AT THE BOTTOM OF THE DEWATERING UNIT of BSM2N
The Benchmark Simulation Model no2 for Nitrous oxide and Complete Autotrophic Nitrogen Removal (the BSM2NplusCANR)
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Steady state predictions by BSM2N
6 21 July 2015
41.22%
13.4%
45.4%
0.01% 0.02%
41.19% NO N2O N2
TNIN TNeff
TNsludge
HOW THE UNCERTAINTY IN MODEL PARAMETERS AFFECT
THE PREDICTIONS?
ASMG1
UNCERTAINTY AND SENSITIVITY ANALYSES
19.5%
23.2%
0.13%
1.7%
0.9%
NO3-
N2
NORG
NPART,INORG
NH4+
[O2]AER1,2,3=2 mg.L-1
TNgas
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Uncertainty and sensitivity analyses on BSM2N predictions
7 21 July 2015
PERTURBATION OF MODEL PARAMETERS
5% variation on GROWTH YIELDS
25% variation on GROWTH/DECAY RATES, N CONTENTS
50% variation on INHIBITION AND HALF-SATURATION PARAMETERS 100% variation on INHIBITION AND HALF-SATURATION PARAMETERS OF AOB-MEDIATED N2O-PRODUCTION PROCESSES STEADY-STATE SIMULATIONS OF THE BSM2N
[O2]AER1,2,3=2 mg.L-1
[TSS]AER3=4000 mg.L-1
PREDICTED TN FLUXES PREDICTED O2 CONSUMPTIONS
Effect on:
PREDICTED N2O EMISSIONS
+SEASONAL
EFFECT on N2O
T=12oC T=15oC T=20oC
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Uncertainty of TN fluxes
8 21 July 2015
units µ σ σ/µ 95th
percentile overall TN stripped [%] 27.09 4.09 0.15 33.8
TN sludge [%] 16.35 2.07 0.13 19.7 TN reject [%] 23.56 2.03 0.09 27
TN removal efficiency [%] 0.64 0.05 0.07 0.7 NO3
- effluent [g.m-3] 16.06 2.07 0.13 19.3 NH4
+ effluent [g.m-3] 0.09 0.05 0.53 0.2
LOW UNCERTAINTY ON TOTAL NITROGEN FLUXES
T=15oC
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Uncertainty of O2 consumptions
9 21 July 2015
units µ σ σ/µ 95th prcl specific O2 consumtpion [g O2,cons.g-1 TNrem] 11.65 1.03 0.09 13.4
O2 cons. by HB [kg O2,cons.d-1] 2847 225.4 0.08 3189 O2 cons. by AOB [kg O2,cons.d-1] 2974.1 61.1 0.02 3069 O2 cons. by NOB [kg O2,cons.d-1] 1116 116.2 0.10 1314
total O2 consumption [kg O2,cons.d-1] 6937 274 0.04 7419
LOW UNCERTAINTY ON OXYGEN CONSUMPTIONS
T=15oC
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Uncertainty of N2O emissions
10 21 July 2015
T=15oC units μ σ σ/μ 95th prct
N2OANOX1 per N2Otot [gN2Otank1.g-‐1N2Otot] 0.05 0.02 0.45 0.09 N2OANOX2 per N2Otot [gN2Otank2. g-‐1N2Otot] 0.05 0.02 0.46 0.09 N2OAER1 per N2Otot [gN2Otank3. g-‐1N2Otot] 0.85 0.05 0.06 0.90 N2OAER2 per N2Otot [gN2Otank4. g-‐1N2Otot] 0.04 0.03 0.67 0.08 N2OAER3 per N2Otot [gN2Otank5. g-‐1N2Otot] 0.01 0.03 2.74 0.01
T=12oC units μ σ σ/μ 95th prct
N2OANOX1 per N2Otot [gN2Otank1.g-‐1N2Otot] 0.05 0.02 0.42 0.08 N2OANOX2 per N2Otot [gN2Otank2. g-‐1N2Otot] 0.06 0.024 0.44 0.1 N2OAER1 per N2Otot [gN2Otank3. g-‐1N2Otot] 0.82 0.05 0.06 0.9 N2OAER2 per N2Otot [gN2Otank4. g-‐1N2Otot] 0.07 0.03 0.5 0.12 N2OAER3 per N2Otot [gN2Otank5. g-‐1N2Otot] 0.012 0.02 1.3 0.03
T=20oC units μ σ σ/μ 95th prct
N2OANOX1 per N2Otot [gN2Otank1.g-‐1N2Otot] 0.05 0.02 0.44 0.084 N2OANOX2 per N2Otot [gN2Otank2. g-‐1N2Otot] 0.05 0.02 0.046 0.081 N2OAER1 per N2Otot [gN2Otank3. g-‐1N2Otot] 0.86 0.045 0.052 0.92 N2OAER2 per N2Otot [gN2Otank4. g-‐1N2Otot] 0.04 0.03 0.06 0.06 N2OAER3 per N2Otot [gN2Otank5. g-‐1N2Otot] 0.01 0.02 1.7 0.02
LOW UNCERTAINTY ON the N2O EMISSION distribution among the AS tanks
STRIPPING
MOST OF N2O IS EMITTED FROM THE FIRST AEROBIC TANK
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Effect of temperature on N2O emissions
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units µ σ σ/µ 95th prct T=12oC T=15oC T=20oC T=12oC T=15oC T=20oC T=12oC T=15oC T=20oC T=12oC T=15oC T=20oC
N2O AER1 [g N.d-‐1] 719.1 1924.4 1963 2800 11871 12341 3.9 6.17 6.3 1500 1510.8 1437.3
THE UNCERTAINTY OF N2O INCREASES AS TEMPERATURE INCREASES
HIGH UNCERTAINTY IN N2O EMISSIONS
A GENERAL BEHAVIOUR OF N2O EMISSIONS WITH TEMPERATURE VARIATION CAN NOT BE IDENTIFIED
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Sensitivity of TN fluxes
12 21 July 2015
Monte Carlo method
nh nY kh
TN effluent -0.56 0.38 -0.25
STANDARDIZED REGRESSION COEFFICIENTS
nh nY fP
TN stripped 0.53 -0.38 -0.32
iXP fP YH
TN sludge 0.83 0.51 0.15
iXB bH YH
TN reject 0.75 -0.49 0.33
hSS,ANOX
hnh
hNOx red. to N gases
hiXP
hsolids in AS unit
hiXB hN released during sludge stabilization
The key strategy to enhance ηTN is to prov ide HB w i th enough SS
hN rem. through sludge disposal
hQwastage
T=15oC
MODEL
LATIN HYPERCUBE SAMPLING PERTURBATION OF PARAMETERS ACCORDING TO
STARDARDIZED REGRESSION COEFFICIENTS
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Sensitivity of O2 consumptions
13 21 July 2015
fP bH YH
O2 consumption by HB -0.58 0.55 -0.42
fP iXP iXB
O2 consumption by AOB -0.63 -0.42 0.4
KS2 ng2 KOH2
O2 consumption by NOB -0.42 0.25 0.23
nh nY fP
Tot. O2 consumption per unit of TN removed -0.56 0.3 -0.25
Monte Carlo method
STANDARDIZED REGRESSION COEFFICIENTS #fP
$SS from biomass decay $O2 cons. for SS oxid. by HB
#fP $XND from biomass decay
$SNH to be oxidized by AOB
#KS2
$NO3- to NO2
- reduction
$NO2- to be oxidized by NOB
#nh #SS in anoxic zone
hSS oxidation with NOX rather than with O2
NO3--to-NO2
- reduction is the key process
T=15oC
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T=20oC µ(EEi)
KS5 0.39
KS1 -0.27
KOH5 -0.25
ng2 0.17
ng4 -0.13
KNO2 -0.11
T=15oC µ(EE
i)
KS5 0.47
KN2O 0.42
KOH5 -0.34
ng5 -0.28
ng2 0.19
bH,KS3 -0.17
KO2,NOB 0.13
µNOB -0.1
Sensitivity of N2O emissions
14 21 July 2015
MODEL
Perturbation coefficient of the parameters
p is the number of levels of variation of θ
N2O emissions are non-linearizable Total N2O emitted
Monte Carlo method Morris screening method
Elementary effect of parameter θi in a point input-space θr
T=12oC µ(EEi)
µNOB -0.61
KS5 0.42
KN2O 0.41
KOH5 -0.26
KFNA 0.25
KS1 -0.23
KS3 -0.2
KNO2 -0.17
ng2 0.14
KS4 0.13
ng5 -0.13 HB denitritifcation plays a dominant role in determining N2O emissions at T=15oC and 20oC
EMERGING CONTRIBUTION BY NOB ACTIVITY ON N2O EMISSION FOR DECREASING TEMPERATURES
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Steady state predictions by BSM2NplusCANR
15 21 July 2015
PN/A
35.5%
[O2]AER1,2,3=2 mg.L-1
13.4%
16.8%
34.3%
19.5%
12%
0.16%
1.7%
0.9%
NO3-
N2
NORG
NPART,INORG
NH4+
0.004% 0.01%
35.49% NO N2O N2
0.02% 41.22%
!N2O/TNstripped
due to lower stripping
23.2%
!NO3-
due to lower infl. NH4
+ load in AS unit
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Conclusions • novel benchmark simulation models for developement of control strategies for
N2O emissions (BSM2N) and for enhanced TN removal (BSM2NplusCANR) have been built up
16 21 July 2015
• Uncertainty analysis show low uncertainty in the TN fluxes predictions but high uncertainty in N2O emissions
• Sensitivity analysis indicates nh and nY as the most influencing parameters determining the plant TN removal efficiency
• The most influencing parameter on N2O emissions at T=15oC and 20oC is the SS half saturation parameter for N2O-to-N2 reduction by HB (KS5)
• Winter temperatures lead to emerging contribution by NOB activity on N2O emissions
• The implementation of the PN/A reactor leads to a reduction of N2O emitted per unit of TN stripped from the AS unit and to a drastic reduction of NO3
- in the effluent
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Future perspectives
• Performing uncertainty and sensitivity analyses on BSM2NplusCANR predictions
17 21 July 2015
• Including N2O production and emission processes in the side-stream PN/A reactor of BSM2NplusCANR
• Developing control strategies for minimization of N2O emission from both mainstream and side-stream biological treatments
• Validate the control strategy obtained in a real full-scale plant
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THANK YOU FOR THE ATTENTION
18 21 July 2015
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TN fluxes predicted by BSM2N vs BSM2NplusCANR
19 21 July 2015
TN stripped from AS 41.22 % 35.5% TN effluent 45.4 % 34.4% TN sludge 13.4 13.4
TN stripped from PN/A 0 16,8%
10 % MORE TN REMOVED BY INCLUSION OF CANR
TN removed 54.6 % 65.7 %