advanced aeration control systems · 2019-02-27 · (abac) • concept –use an ammonia setpoint...
TRANSCRIPT
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Advanced Aeration Control Systems at Water Resource Recovery Facilities (WRRFs)
Alex Doody CDM SmithPart 1: Purpose of Aeration Control & Overview of Key Components
David WankmullerHazen and SawyerPart 2: Aeration Control Strategies
John Manning Freese & Nichols, Inc.Part 3: Case Study #1: DO-based Aeration Control at SAWS Leon Creek WRC
Eric Redmond Black & VeatchPart 4: Case Study #2: Ammonia-based Aeration Control
Go to weat.org/events to view the webinar, presentation slides, multi-site user
sign in sheets, and webinar questions for CEU credit.
An event from the Municipal Resource Recovery & Design Committee (MRRDC)
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Nick LandesFreese & Nichols, Inc.Moderator
Go to weat.org/events to view
the webinar, presentation slides,
multi-site user sign in sheets,
and webinar questions for CEU
credit.
Advanced Aeration Control Systems at Water Resource Recovery Facilities (WRRFs)
An event from the Municipal Resource Recovery & Design Committee (MRRDC)
![Page 3: Advanced Aeration Control Systems · 2019-02-27 · (ABAC) • Concept –use an ammonia setpoint in the aerobic zone to determine the optimal DO setpoint, typically for nitrification](https://reader034.vdocuments.us/reader034/viewer/2022042100/5e7c6751f4953632ca5d259b/html5/thumbnails/3.jpg)
Part 1: Purpose of Aeration Control & Overview
of Key Components
Alex Doody, P.E.
CDM Smith
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Why Do We Care About Aeration?
#1: Aeration is the beating heart of the activated sludge process
#2: Aeration is the largest consumer of electric power within a WRRF (50-60%)
• High operating cost
• Environmental impact of energy production
55%31%
11% 3%
Aeration Pumping
HVAC & Others Lighting
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Basic Aeration System Components
Air/Oxygen Supply Oxygen Transfer
Mechanical Aeration
+
or
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Geared
Magnetic
Bearing
Air Bearing
Centrifugal
Direct Drive
Multistage Single Stage
Positive Displacement
Rotary
Lobe
Screw
(Hybrid)
Blower Types
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Blower Operations
Variable Speed Drives
(VFDs)
Positive Displacement
Single Stage, Direct Drive
(Turbo)
Multistage Centrifugal
Inlet Throttling
Multistage Centrifugal
Inlet and Outlet Guide
Vanes
Single Stage, Integrally Geared
• Constant speed: simple, but wastes
energy and excess DO can lead to
sludge bulking
• Ways to
vary output
depending
on blower type:
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Process Sensors
Dissolved Oxygen Ammonia Oxygen Uptake Rate
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Advanced Aeration Control
Use of process sensors, automated control valves, and flow meters to match process
oxygen demands to air supply
Blowers
PIT
DO NH3
Aeration
Tanks
MFIT
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Why Advanced Aeration Control?
• When permit limits dictate accurate control for optimal BNR operation
• When energy and other cost savings of advanced control can justify cost of control equipment
Source: Stenstrom and Rosso (2010) www.seas.ucla.edu/stenstro/Aeration.pdf
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Modulating Control Valves
• Can be installed in multiple locations: On header to each treatment train
On each diffuser dropleg
• Many types and styles available, including:
• Actuator type also important
Butterfly Valves Diaphragm Valves Jet Valves
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Source: The Binder Group
Stable Control Range
BFVs: 50-80%
Diaphragm
Valves: 20-90%
Jet Valve: 0-95%
% stroke
% flow
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Recently Commissioned Diaphragm Valves at a 36 mgd WRRF
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Air Supply Monitoring
Air flow meters: • Can be provided on blower discharge header or
on individual diffuser droplegs
Pressure transmitters: • Typically installed on blower discharge header
• Rising pressure over time indicates when diffusers need to be cleaned
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Ammonia Instrument Types
TypeIon Selective Electrode
ProbesWet Chemistry Analyzers
Range
Nominally 0 – 1,000 mg/L N
Typ calibrated around 1 – 20
mg/L N
Nominally 0.02 – 1,000 mg/L N
Typ calibrated around 0.05 – 20 mg/L
N
Accuracy ± 5% of mV signal + 0.2 mg/L ± 3% + 0.05 mg/L
Source: Hach CompanySource: Upper Blackstone Clean Water
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Ammonia Instruments for ABAC: Lessons Learned
Ion Selective ElectrodeProbes
Wet Chemistry Analyzers
Low Ammonia
Often struggle in low ammonia
environments (< 1 mg/L NH4-N)
Better choice for locations with
< 1 mg/L NH4-N
Location
Most common in first half of
tank (anaerobic/anoxic or head
of aerobic)
Mixed success for primary
effluent (due to grease)
Most common at end of aerobic zone,
secondary effluent, final effluent
Mixed success in upstream locations
(small tubing turns black)
Accuracy Checks
Require frequent accuracy
checks and re-calibration
Accuracy checks recommended to
identify when maintenance required
on tubing or flow cells
O&M
Replacement cartridge heads
can be costly if required multiple
times/year
Reagent cost can be reduced by
increasing time interval (balanced
with process control needs)
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Why not just “Keep it Simple ___”?
1. If energy or other cost savings can justify cost of control equipment
2. When permit limits dictate accurate control for optimal performance (important for BNR systems especially)
3. Process performance trending, which provides data useful for trouble-shooting when problems arise
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Well-Designed Aeration Controls Will:
1. Achieve process set point (DO typically) quickly and maintain set point under variable loading conditions
2. Maintain set points with as few equipment starts/stops as possible (blowers, valve actuators)
3. Optimize energy use by minimizing air flow needed for process needs and by reducing pressure loss
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Part 2: Aeration Control System Strategies
Dave Wankmuller, P.E.
Hazen and Sawyer
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Outline
• DO – Based Aeration Control– DO control with mechanical aeration– DO Control with diffused aeration and blowers
• Tapered diffuser layout• Control with:
– Blower modulation ONLY– Airflow based control– Pressure based control
• Most Open Valve automated control types
• Ammonia-Based Aeration Control (ABAC)– Why might consider (energy/BNR process control)– Types of ABAC
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Mechanical Aeration
• Many different types:
– Vertical/Horizontal
• Platform mounted – Submerged/Surface
• Floating Aerators – Aspirating/Non Aspirating
Corgin.co.uk waterworld PP Aquatech
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Mechanical Aeration Control Techniques
• Variable water level– Effluent weir or slide gate adjusted to raise or lower
surface level– As submergence decreases, the OTR (and power draw)
decreases*
• Variable speed– As speed of aerator is reduced, the OTR decreases*– Typically Implemented with VFDs– Must maintain mixing
• Variable operating time– Cycle units on and off based on DO setpoints
*Note: relationship between varying water level/speed may not be linear to OTR
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Blowers & Diffused Aeration
• Tapered diffuser layout
• Control with:
– Blower modulation ONLY
– Airflow Based Control
– Pressure Based Control
• Most Open Valve automated control types
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Tapered Aeration
• Reducing the number of diffusers per ft2 SA traveling down tank
• Diffusers are typically tapered based on the anticipated OUR through the basin
• Highest oxygen demand at the head of the basin – Need more air and/or higher
density of diffusers in that zone
FLOW
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Tapered Aeration
Image: Jenkins
• Up to 50% of the aeration demand can be in the first 20% of the basinOUR Calculations:• OUR Can be estimated with modeling software• Site specific OUR can be determined with offgas testing
• As you travel down the basin
• Oxygen Demand decreases
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Tapered Aeration
• Tapering diffusers is necessary to achieve even DO distribution throughout the tank
• Theoretically if DO probe is located at the end of the tank
– Under design load conditions do in the entire basin should be 2.0 mg/L. DO Probe
setpoint 2.0 mg/L
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Blower Modulation Only
Blower
Diffusers
Air Piping
Aerobic Reactor
• Modulate airflow from the blower using:– VFD
• PD, Turbo, Multi-stage
– Inlet Throttling• Multistage
– Guide Vanes• Single-stage IG
• Increase Airflow to Increase DO, and vice versa– Or if blower is at full capacity, increase # of blowers online
DO Probe
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Airflow Based Control
• PID feedback loop
– Airflow is the process variable
– Valve position is the manipulated variable
• Program looks at three variables
– DO error – how far is the program from the DO setpoint
– Airflow Setpoint (Calculated Value)
– Actual Airflow (Read at the airflow meter)
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Simplified Airflow Control Aeration Diagram
DO Probe
Airflow Meter
Airflow Control Valve
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Pressure Based Control
• Maintain a specific header pressure
– Cascade Loop
• Loop 1 – DO controlled based on modulating control valves
• Loop 2 – Maintains pressure in main header by increasing/decreasing blower speed/inlet valve position
• Implemented since the 1960s
– Most controllers were single loop PIDs
• If tuned incorrectly, valves and blower speed can oscillate around setpoint (hunting)
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Simplified Pressure Based Aeration Diagram
DO Probe
Pressure Indicator
Airflow Control Valve
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Most Open Valve Control
• Modification to previous control loops to reduce discharge pressure (and therefore energy)
• One of the aeration control valves shall be at the “maximum” position at all times – This is the “most open valve”
• Flow Based Control– Once a valve achieves “most open valve” position – it is locked in that
position• Other valves modulate based on DO requirements• Eventually a second valve will achieve “most open valve” position and the first
valve will be allowed to close
• Pressure Based Control – Program re-adjusts the pressure setpoint based on valve position– If one valve is at maximum, but not achieving DO setpoint, increase
pressure setpoint (0.05 – 0.1 psig)
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Ammonia Based Aeration Control (ABAC)
• Concept – use an ammonia setpoint in the aerobic zone to determine the optimal DO setpoint, typically for nitrification
Blower
Diffusers
Air Piping
Aerobic Reactor
Control Algorithm Controller
DO NH3
Simplified Control Algorithm:• Operator selects effluent ammonia set-point• When effluent ammonia is greater than set-point, controller increases DO• When effluent ammonia is below set-point, controller decreases DO
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Types of ABAC
• Directly control airflow based on ammonia concentration• Cascade control
– Control DO conc. based on desired ammonia conc. airflow adjusts to maintain DO concentration
• Feedforward– Ammonia probe at the head of the aerobic zone, program calculates
airflow necessary for nitrification
• Feedback– Ammonia probe at the end of the aerobic zone, program decreases DO
if below setpoint and increases DO if above setpoint
• Feedforward and feedback– Ammonia probe at beginning and end of zone, calculates air necessary
for nitrification, corrects based on the ammonia probe reading at the end of the zone.
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Why ABAC?
• Ensure nitrification by the end of the aerobic tank– Help meet NH3 permit limit
– Sometimes a basin needs a DO above a typical setpoint of 2.0 mg/L to achieve full nitrification
• Optimize nitrogen removal efficiency– Supplying the amount of air necessary for nitrification (no
more, no less)
– For facilities that denitrify and have a second anoxic zone -reduces carbon usage due to less DO entering anoxic zones
• Minimizes airflow and energy use– Only supplying the air you need = less energy usage
• Maximize simultaneous nitrification and denitrification (SND) at low DO concentrations
– For low TN facilities – SND encourages nitrification and denitrification to occur in the same zone
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The Objective of ABAC is to Use the Entire Aerobic Volume to Remove NH3
NH3 level in basin
Plug Flow Aeration BasinInfluent Effluent
Airflow
Too much air- Energy consumption- Carbon oxidation
NH3 level in basin
Airflow
Not enough air- High effluent ammonia
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ABAC
• Operator selects effluent ammonia set-point
• When effluent ammonia is greater than set-point, controller increases DO
• When effluent ammonia is below set-point, controller decreases DO
NH3 level in basin
Plug Flow Aeration BasinInfluent Effluent
Airflow
Just right
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Part 3: Case Study #1: DO-based Aeration Control at
SAWS Leon Creek WRC
John Manning, P.E.
Freese & Nichols, Inc.
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Case Study
• SAWS Leon Creek Plant
– Take an alternative interactive approach for the design of an automated Dissolved Oxygen control system at the aeration basins
• SAWS operators
• Maintenance staff
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Topics
• Design Coordination
• Construction Coordination
• Training
• Testing
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SAWS Leon Creek WRC
• Conventional activated sludge plant
– Peak capacity of 92MGD
– Average daily flow rating of 46MGD
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15 AERATION BASINS
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SAWS Leon Creek WRCProject Goal
• Ease operations with the automation of 15 aeration basins
– Modify manual air flow control valves to motorized modulating flow control
– Add air flow meters to each basin
– Add D.O. analyzers to each basin
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Modified Design Steps
• SAWS requested workshops in the Engineering scope– Workshops Included
• Aeration basin maintenance and controls considerations with plant staff early in design
• Controls review– Design
– Construction
• Milestone reviews– Design
• Training– Construction
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SAWS Operations Requests
• Simplified system
– Automatic mode
– Manual mode
– Service mode
• Simplified graphics
– Show status of each mode on same screen
• Make process troubleshooting manageable and flexible
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Construction Interaction
• Review HMI screen development– DCS
– Aeration Basin Control Manufacturer
• Testing– 100 hour run test
– 30 day acceptance tests
• Training– Manufacturer provided with support from Engineers
– Operator put their hands on the systems while the instructor and engineering is there
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Results
• Keeping operations involved from design through construction can positively affect end results
• Transitioning to the automated system was easier since hands on training was available
• An operator thanked SAWS Project Manager for providing a simple system
• Maintaining engineer staff involvement throughout the projects life was beneficial to operations
• Metric ---- Two Thumbs up!!
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Part 4: Case Study #2: Ammonia-based Aeration
Control
Eric Redmond, P.E.
Black & Veatch
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Timeline to aeration implementation
2012 2013 2014 2015 2016 2017 2018
Demonstration
basin
commissioned
Full plant low DO
testing
Partial “A Section
Off” Testing
Full plant
“A Section Off”
Full scale BNR design started
First BNR basins
commissioned
Planning
Field Testing
Modify
Full-Scale
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Full Scale Testing
0
0.5
1
1.5
2
2.5
3
3.5
A B C
DO Setpoint (mg/L)
Aeration Basin Section
ConventionalDO
Low DO
40,000
50,000
60,000
70,000
80,000
90,000
100,000
9/1/2012 10/31/2012 12/30/2012
TotalAirflow(scfm)
All operating basins in low DO mode
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Are there major risks that need to be mitigated during design?
Dots = 24 hr composite
Simulated Ammonium
Concentration
mg N/L
Systematic increasing of load during winter
conditions simulated under design
conditions
Largest risk: sensitivity to ammonium loads Low DO setpoint
decrease rate
Still same mass of bacteria, just slowed down
Increase DO, increase rate to a certain point
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Project Objective
Objective: Implement ammonium based airflow control (ABAC)
Goals:a. Reduce aeration energy
b. Improve process controls and monitoring
c. Meet effluent NH4 requirements
d. Implement selector zones
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Control Scheme
Ammonium SensorD.O. Sensor
1. Ammonium reading
determines D.O. setpoints
Air Piping Flow Meter +
Valve
Pressure
Gauge
2. D.O. reading determines
valve position
3. Valve position
impacts system
press
Ammonium Based Aeration Control (ABAC)
Ammonium sensor accuracy is critical
Zone Low DO,
mg/L
High DO,
mg/L
A1 0.3 0.3
A2 0.5 0.5
B 0.9 1.5
C 1.2 1.7
Target NH4 1.0
Example SetpointsTypical DO Control Scheme
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Diffusers, Selector Zone, and ABAC
• 48 DO sensors
• 12 TSS
• 12 pH
• 12 Ammonium
• 12 ORP
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STARTUP AND OPTIMIZATION
Data Analysis
• Assess performance
• Tuning and balancing
• Set point guidance
Field Evaluation
• Probe calibrations
• Training on probe accuracy
Modeling Support
• Performance validation
• Training tool
Stable Advanced Process Control
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Operations Optimization
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Consistent operation between zones
• Zones A1 and
A2 greatly
impact
downstream
Zone B
• All zones should
be similar to
Zone C with no
trend
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How well are the NH4 probes performing?
Probe values closely matching trend of effluent data
Effluent lab data typically 1-2 mg N/L lower
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Is it worth it?
Predicted annual costs
InfrastructureAnnual Cost1
($/year)% Annual Savings
Pre-Construction $1,275,930
31%Post-Construction $875,360
Total Difference $400,570
1 Costs were developed assuming 28 scfm/HP and an electricity rate of $0.055 /kWh.
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Lessons Learned
• Operations and maintenance training
• Demonstration testing
• Open communication
• Data review and analysis
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CEU Questions
1. Oxygen demand is the highest at the head of the aeration basin
a) True
b) False
2. Modulating airflow from a blower can be done using:
a) Variable Frequency Drives (VFDs)
b) Inlet Throttling
c) Inlet and Outlet Guide Vanes
d) All of the Above
3. Ammonia-based Aeration Control (ABAC) system uses an effluent
ammonia set point to determine the optimal Dissolved Oxygen
(DO) required for nitrification:
a) True
b) False
Go to weat.org/events to view the
webinar, presentation slides, multi-
site user sign in sheets, and
webinar questions for CEU credit.
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Advanced Aeration Control Systems at Water Resource Recovery Facilities (WRRFs)
Alex Doody CDM SmithPart 1: Purpose of Aeration Control & Overview of Key Components
David WankmullerHazen and SawyerPart 2: Aeration Control Strategies
John Manning Freese & Nichols, Inc.Part 3: Case Study #1: DO-based Aeration Control at SAWS Leon Creek WRC
Eric Redmond Black & VeatchPart 4: Case Study #2: Ammonia-based Aeration Control
Go to weat.org/events to view the webinar, presentation slides, multi-site user
sign in sheets, and webinar questions for CEU credit.
An event from the Municipal Resource Recovery & Design Committee (MRRDC)