membrane bioreactor pilot plant operating...
TRANSCRIPT
Membrane Bioreactor Pilot Plant Operating Experience
Pardi SukapanpotharamBob Bucher
King CountyTechnology Assessment Program
Impact of Mixed Liquor Characteristics on Filtration
Presentation Objectives
Share the experience of operating a pilot MBR plant. Present water quality and
biological process parameters and corresponding filtration performance.
Pilot Information Pilot provided by Enviroquip, Inc. Pilot equipped with Kubota plate
membranes. Operated at the West Point
Treatment Plant from 2004 – 2006. Total process volume of 9,000 gal Treatment capacity of 40,000 gal/d
Membrane Specifications
200 plates (EW 200) Surface area = 13.45 ft2/plate Nominal net flux = 14.7 gfd Nominal pore size = 0.4 micron Effective pore size = 0.1 micron
Pilot Process Flow Diagram
Feed
EffluentSample
AnoxicAerobic/
Membrane
2 mm bandscreen
Turbidimeter
Filtrate
WasteSludge
Blower
C
6 mmscreen
S50S54
S53
S52
S51
Pre-Aeration
Mixed Liquor Recycle (via gravity flow)
C
Pilot Installation
Pilot Operating Conditions Nominal net flux = 14.7 gfd Relax frequency = 9 min Relax duration = 1 min Specific air scour = 0.017-0.026 scfm/ft2
MLSS = 8,000 – 15,000 mg/L ML recycle ratio = 2 – 6 Feed = primary influent or primary
effluent
Testing Phases Baseline Long term flux increase (125% of
nominal flux for 1 month) Diurnal flow 24-hrs peak event 72-hrs peak event Polymer addition
Disruptions in Pilot Operation Process re-seeding Revisions to membrane control logic Inspection of membrane cartridges Replacement of membrane cartridges Replacement of ML recycle pumps Replacement of aeration blowers Loss of power to West Point pilot facility
Operational Comparison(MBR vs. CAS)
Both rely on good biological process control Physical barrier vs. gravity settling Loss of treatment capacity vs. solids
carry-over MBR parameters:
•Flux = flow/area (gal/ft2/d)•TMP = trans membrane pressure (psi)•Permeability = flux/TMP (gfd/psi)
Membrane Fouling Reduction of pore size or effective filtration
area Additional energy required to pull water
through the membrane characterized by:• Increase in trans membrane pressure (TMP)• Decrease in permeability (flux/TMP)
Increases over time Response to fouling:
• Increase relax frequency• Increase air scour• Chemical cleaning
Factors Impacting Characteristics of Biological Process Solids (ML)
Feed characteristics Process Temperature DO pH Hydraulic retention time Solids retention time
Biological Parameters Impacting Membrane Fouling Potential
Mixed liquor concentration Viscosity Temperature Soluble microbial products (SMP) Colloidal material
MBR Process Optimization
Biological Membrane
Pilot Biological Process Monitoring Parameters
SRT MLSS/MLVSS sCOD Temperature pH DO F/M
Nitrification Filterability Specific Oxygen
Uptake Rate Microscope
Inspection
Pilot Membrane Process Monitoring Parameters
TMP/Permeability Air scour flow Effluent turbidity Cycle length (permeate/relax) Recycle flow Permeate flow Temperature
Pilot Field Testing Filterability (Time to Filter) Viscosity Capillary Suction Test (CST) DO Temperature pH Specific Oxygen Uptake Rate (SOUR) Visual inspections (air scour)
MBR Pilot Data Sample
MBR Pilot Data Review(Mixed Liquor Suspended Solids)
0
5
10
15
20
25
30
35
40
45
5019
-Jul
-05
21-J
ul-0
5
23-J
ul-0
5
25-J
ul-0
5
27-J
ul-0
5
29-J
ul-0
5
31-J
ul-0
5
2-A
ug-0
5
4-A
ug-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
0
2,000
4,000
6,000
8,000
10,000
12,000
14,000
16,000
18,000
20,000
MLS
S (m
g/L)
Lower deck permeabilityUpper deck permeabilityMLSS (mg/L)
MBR Pilot Data Review(Permeability and SOUR)
0
10
20
30
40
50
605-
Oct
-05
25-O
ct-0
5
14-N
ov-0
5
4-D
ec-0
5
24-D
ec-0
5
13-J
an-0
6
2-Fe
b-06
Date
SOU
R (m
g/gV
SS/h
r)
Per
mea
bilit
y (g
fd/p
si)
SOURLower PermeabilityUpper Permeability
Pilot Operating Conditions for Data Presented in Following Slides
Sep 18 – Dec 8, 2005 •Average Temp = 18ºC (13-22ºC)•Average Air Scour = 0.022 scfm/ft2•Average Flow = 28 gpm•Average MLSS = 12,000 mg/L
MBR Pilot Data Review( F/M )
020
4060
8010
012
014
05-
Sep-
05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-No
v-05
14-N
ov-0
5
24-N
ov-0
5
4-De
c-05
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
0.00
0.02
0.04
0.06
0.08
0.10
0.12
0.14
F/M
ratio
(1/d
ay)
Lower PermeabilityUpper PermeabilityF/M ratio
cleaningFlow = 20 gpm
MBR Pilot Data Review( SRT )
020
4060
8010
012
014
05-
Sep
-05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-N
ov-0
5
14-N
ov-0
5
24-N
ov-0
5
4-D
ec-0
5
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
0
5
10
15
20
25
30
35
SRT
(day
s)
Lower Permeability
Upper Permeability
SRT
MBR Pilot Data Review( Filterability )
020
4060
8010
012
014
05-
Sep
-05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-N
ov-0
5
14-N
ov-0
5
24-N
ov-0
5
4-D
ec-0
5
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
0
2
4
6
8
10
12
14
16
18
20
Filte
rabi
litly
(mL/
5min
)
Lower Permeability
Upper Permeability
Filterability
MBR Pilot Data Review( sCOD )
0
20
40
60
80
100
120
1405-
Sep
-05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-N
ov-0
5
14-N
ov-0
5
24-N
ov-0
5
4-D
ec-0
5
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
Lower Permeability Upper Permeability sCOD in mixed liquor
MBR Pilot Data Review( CST )
020
4060
8010
012
014
05-
Sep
-05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-N
ov-0
5
14-N
ov-0
5
24-N
ov-0
5
4-D
ec-0
5
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
0
5
10
15
20
25
30
35
Cap
illar
y Su
ctio
n Te
st (s
ec)
Capillary Suction Test
Upper Permeability
Filterability
MBR Pilot Data Review(Nitrification)
0
20
40
60
80
100
120
1405-
Sep-
05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-N
ov-0
5
14-N
ov-0
5
24-N
ov-0
5
4-D
ec-0
5
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)
Lower Permeability (gfd/psi)Upper Permeability (gfd/psi)Ammonia Removal
MBR Pilot Data Review(COD Removal)
0
20
40
60
80
100
120
140
5-Se
p-05
15-S
ep-0
5
25-S
ep-0
5
5-O
ct-0
5
15-O
ct-0
5
25-O
ct-0
5
4-N
ov-0
5
14-N
ov-0
5
24-N
ov-0
5
4-D
ec-0
5
14-D
ec-0
5
Date
Perm
eabi
lity
(gfd
/psi
)CO
D re
mov
al (%
)
Lower Permeability (gfd/psi)Upper Permeability (gfd/psi)COD Removal
Membrane Fouling Control
Decrease flux Increase specific air scour Increase relax frequency Increase chemical cleaning
frequency Polymer addition
Membrane Fouling Control (Flux Decrease)
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
0 2 4 6 8 10 12 14 16
Flowrate (gfd)
TMP
(psi
)
Air = 0.02 scfm/sfTemp = 11 CMLSS = 11,767 mg/L
Membrane Fouling Control (Pilot Example – Flux Decrease)
Dec 15, 05
0
5
10
15
20
25
30
35
12/1
5/05
19:
12
12/1
5/05
19:
26
12/1
5/05
19:
40
12/1
5/05
19:
55
12/1
5/05
20:
09
12/1
5/05
20:
24
12/1
5/05
20:
38
12/1
5/05
20:
52
12/1
5/05
21:
07
12/1
5/05
21:
21
12/1
5/05
21:
36
12/1
5/05
21:
50
12/1
5/05
22:
04
12/1
5/05
22:
19
12/1
5/05
22:
33
12/1
5/05
22:
48
12/1
5/05
23:
02
12/1
5/05
23:
16
12/1
5/05
23:
31
12/1
5/05
23:
45
12/1
6/05
0:0
0
Time
Flow
(gpm
) & T
MP
(psi
)
Lower flow (gpm)Upper flow (gpm)lower TMPupper TMP
Membrane Fouling Control (Air Scour Rate Increase)
0.0
0.2
0.4
0.6
0.8
1.0
1.2
1.4
0 2 4 6 8 10 12 14 16
Flowrate (gfd)
TMP
(psi
)
0.02 scfm/sf0.014 scfm/sf
Membrane Fouling Control(Pilot Example -Polymer Addition)
0
10
20
30
40
50
60
70
80
901/
17/0
6 9:
36
1/17
/06
10:4
8
1/17
/06
12:0
0
1/17
/06
13:1
2
1/17
/06
14:2
4
1/17
/06
15:3
6
Perm
eabi
lity
(gfd
/psi
)
Lower PermeabilityUpper permeability
Before Polymer AdditionFilterability = 1.6 ml/5min
After Polymer AdditionFilterability = 20 ml/5min
Presentation Summary During piloting, several parameters were
typically changing at the same time – difficult to establish performance relationships.
Membrane fouling will occur under all operating conditions.
Multiple parameters must be monitored simultaneously for troubleshooting and maintenance of filtration process.
Need to find practical methods for utilizing membrane fouling research data.
Acknowledgements Kubota Membrane Corporation
Enviroquip, Inc.
West Point Treatment Plant Staff
King County Environmental Lab Staff
Membrane Bioreactor Pilot Plant Operating Experience
Pardi SukapanpotharamBob Bucher
King CountyTechnology Assessment Program
Impact of Mixed Liquor Characteristics on Filtration