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• Aqua-Aerobic Systems – KMS Partnership
• Traditional MBR Approach
• Aqua-Aerobic Time-managed Biological Approach
• Bioreactor Operation & Membrane Integration
• Traditional Membrane Issues
• KMS Puron® Membrane Technology
• Membrane Module Design & Construction
• Membrane Cleaning Operations
Aqua-Aerobic™ MBR Topics
AquaSBR®
1986
Aqua MSBR®
1991
AquaMB Process®
2003
Aqua-Aerobic® MBR
2005
MBR Pilot
Rockton Illinois
1999
MB Pilot
UC Davis
2002
Aqua Aerobic: Membrane Development
Aqua-Aerobic MBR™ Membrane Bioreactor
•Integrates PURON®
Submerged Membranes
Into An Aqua-Aerobic
Time-Managed
Biological Process
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
Aqua-Aerobic® MBR Home
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Aqua Aerobic MBR System Overview
A. Headworks
• Coarse Screening (6 mm, ¼”) – Optional?
• Grit Removal – Optional?
• Fine Screening (1-3 mm) – Required!
B. Biological Process
• Time Managed Processes
• MLSS = 8,000-10,000 mg/l
C. Membrane Filtration
• Puron™ Submerged Membranes
• 0.05 Micron Filtration
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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• Sequencing Batch Reactor (batch)
• Phased Activated Sludge (continuous)
Aqua-Aerobic® MBRTreatment Modes
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
Aqua-Aerobic® MBR Home
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AquaSBR System
• 20+ Years & >900 Installations
• Best Lifecycle Costs of Activated Sludge
• Proven BNR Performance
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Typical MBR
BNR (Denitrification & P Removal)
Anaerobic AnoxicAerobic
10,000 mg/l
Membranes
Membranes
1Q
4Q
3-4 QPURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Effluent NO3-N vs. Recycle Rate
1,800%
0%
200%
400%
600%
800%
1,000%
1,200%
1,400%
1,600%
0 2 4 6 8 10
Desired Effluent Nitrate Concentration (mg/L)
Req
uir
ed
Rec
yc
le F
low
Rate
(Perc
en
t o
f in
flu
en
t fl
ow
)
Internal N03-N Recycle Pump Not Required with Aqua-Aerobic® MBR!
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Typical MBR
BNR (Denitrification & P Removal)
Anaerobic AnoxicAerobic
10,000 mg/l
Membranes
Membranes
1Q
4Q
3-4 QPURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Multi-Stage MBR
Common Issues relating to BNR:
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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1. Design suited for all conditions:
• 100% of Design
• Initial Conditions (5-25% of Design)
2. Nitrate Control
• Excessive DO in Membrane Tank Recycle
• Improper return of RAS (to Anaerobic/Anoxic)
• Actual Detention Time in unit Processes (RAS)
• Mixing with Aeration in Aerobic Tanks
SBR2
10,000 mg/l
Membranes
Membranes
4Q
SBR1
10,000 mg/l
Aqua Aerobic® MBR Process
Simplified Process Flow
•Reduced Internal Recycle (3-5Q) for BNR
•Reduced Unit Processes
•Time-Managed/Controlled Bio-Process
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Conventional AquaSBR® Cycle Structure
Metal Salt Addition (for TP < 1 mg/l)
Phases Not Required in
Aqua-Aerobic® MBR
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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AquaSBR System –With Membranes
Volume Reduction Advantage
1. Full Utilization (24 hours/day) of Aeration/Mixing
a) Settle & Decant Phases Not Required
b) Adds 33-38% to actual Treatment Cycle
2. Elevated MLSS from 4,500 mg/l to 10,000 mg/l
3. Reduced Cycle Duration
a) More, but smaller batches (from 5 to 12 cpd)
Aqua-Aerobic® MBR: DesignGeneral Arrangement
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Flux Control: Design ConditionsInherent Equalization
React Fill React Draw
Anaer. O2 Anox O2 O2Anox
Max Design Flow
Ave Design Flow
Fmax
Fopt
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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SBR2
10,000 mg/l
Membranes
Membranes
4Q
SBR1
10,000 mg/l
Aqua Aerobic® MBR Process
Continuous-Flow, Batch ReactionTime: 0 to 60 minutes
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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SBR2
10,000 mg/l
Membranes
Membranes
4Q
SBR1
10,000 mg/l
Aqua Aerobic® MBR Process
Continuous-Flow, Batch ReactionTime: 60 to 120 minutes
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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React Fill React Draw
Anaer. O2 Anox O2 O2AnoxReactor 1
React FillReact Draw
Anaer. O2 AnoxO2 O2AnoxReactor 2
Batch Treatment ModeDual-Basin Relationship
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Batch Treatment ModeStart Mixed Fill – LWL
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Batch Treatment ModeEnd React Fill – HWL
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Batch Treatment ModeStart React Draw – HWL
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Batch Treatment ModeEnd React Draw – LWL
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Aqua-Aerobic® MBR Animation
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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React Fill React Draw
Anaer. O2 Anox O2 O2Anox
Fopt Fzero Fopt
Flux Control: Initial Plant Flow
• Optimal Flux Used For Membranes
• Relaxation During Anoxic Stage, Recycle From MT Eliminated
• No Oxygen Input From Air Scour During Anoxic StagePURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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• Superior Management Of Process Environment
• Lowest Energy Cost Of Membrane-coupled
BNR Systems
• Inherent Hydraulic & Constituent Equalization
• Predictive Sludge Feed To Membrane Tank
• Proven & Reliable Nutrient Removal
Performance
• SCADA & Instrument Friendly Process
(Intellipro® Ready)
Aqua-Aerobic® MBR AdvantagesBiological Portion
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Aqua-Aerobic® MBR: DesignMembrane Tank
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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PURON® Membrane Technology
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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•Membrane Filtration
−Local dewatering of the
sludge
−Concentration of solids in
module may lead to
blocking of module
•Design Goals
−Safe flushing of solid
matter out of module
−Robust design to minimize
problem components
(hairs, fibers, ...)
•Solids Management
PURON® Membrane TechnologyIdentifying Process Issues
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Clogging
Clogging by hairsand fibrous materialat the upper end
Sedimentation of sludgein poorly aerated
potting area
Sludging Filtrate
Consequence = reduced filtration rate
PURON® Membrane TechnologyPerformance Challenges – Double Header Design
Edge clogging
Low flow rate on
the edges leads
to clogging
Gap clogging
are susceptible
plate gaps
to clogging
Uneven
Resulting in: high aeration rates
PURON® Membrane TechnologyPerformance Challenges – Panel (Flat Sheet) Membranes
fiber cages
air injectionmodule-
element
filtratefiltrate
PURON – module row
Filtrate
Individually Sealed
Hollow Fibers
One side potting
Central air injection
+
Reduced clogging and sludging
Reduced energy consumption for aeration
main advantages
PURON® Membrane TechnologyDesign Issues – Single Header Concept
Air Supply
Module Rows
Air Distribution
FiberSupport
PermeateRemoval In Each
Row
Permeate
Permeate Collector
Open End FibersIndividually
Sealed
ModuleFrame
MountingDevice
PURON® Membrane TechnologyModule Unit Construction
10 µm
2 µm 2 µm 2 µm 2 µm 2 µm
Membrane Cross Section
Enlargement: 10,000 x
Braided Support Membrane Surface
Supported Hollow Fiber
2.6 mm
Filtrate
Mixed
Liquor
PURON® Membrane TechnologyHollow Fiber Design & Construction
5,400 ft2 (500 m2) Module
Module Designation
PURON A30HS PURON A235HS PURON A500HS
Length (ft) 0.75 3.5 6.6
Width (ft) 3.3 3.3 3.3
Effective Fiber Length (ft) 5.9 5.9 5.9
No. of Rows 1 8 17
Bundles per Row 9 9 9
Surface Area (m2) 30 m2 235 m2 500 m2
Dimensions
PURON® Membrane TechnologyModule Standard Models
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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• Sludge-side air scouring, continuous or intermittent
Three cleaning methods to maintain permeability:
• Permeate backflush
• Chemical cleaning, in intervals or operational related
Aqua-Aerobic® MBRCleaning Methods
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
Aqua-Aerobic® MBR Home
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0
-10
-20
-30
10
20
30
40
50
Flu
x (
lmh)
60 120 180 240 300 360 400
Time (sec)
BackwashingGross Flux vs. Net Flux
1. Maintenance Cleaning (In-Situ)
– Typical chemicals include NaOCl and Citric Acid
– NaOCl Concentration: 500 – 1000 ppm
– Citric Acid Concentration: pH = 3
– Backflush at 3 – 6 l/m2/hr during dosing for 30-45 minutes
for each chemical
– Ideally, each 2-3 weeks - Automated
2. Recovery Cleaning
– Same chemicals
– NaOCl Concentration: 2,000 ppm
– Citric Acid Concentration: pH = 3
– Sludge drained and membranes submerged in chemicals
– Approximately 24 hours for entire process
– Ideally, each 6-12 months – Semi Automated
Aqua-Aerobic® MBR Chemical Cleaning Methods
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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Aqua-Aerobic® MBRPilot Plant
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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• Single Header Design – Reduced Clogging
• Sludge Side Air Scour – Reduced Sludging
• Automatic Permeate Backflush
• Reinforced, Braided Fiber
• Lower Pre-Treatment Dependency
• Automated In-situ Chemical Cleaning
• Standard Sizes For Submerged Models
Aqua-Aerobic® MBR AdvantagesMembrane Portion
PURON® Technology
Aqua-Aerobic® MBR
Advantages
Cleaning Methods
Phases of Treatment
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