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Aeration Control and Energy Cost Reduction

​Statement of the Problem

One major use of energy in a wastewater treatment facility is for operation of mechanical systems designed to introduce oxygen into the wastewater. This oxygen is necessary for biological treatment of carbonaceous matter (secondary treatment) and for oxidation of ammonia into nitrite and nitrate (nitrification). The transfer of oxygen can be accomplished by several methods. One method is the delivery of air through a network of pipes and diffusers located at the bottom of treatment basins (diffused aeration). Another method is the high speed operation of brushes, paddles and/or other mechanical arms at or near the surface of the wastewater (mechanical mixing).

A difficult control challenge is at plants that require nitrogen removal under variable flow and/or variable ammonia demand conditions. At some locations, influent ammonia delivered to the aeration basin for treatment is disproportionate to flow and highly variable throughout the day and throughout the week. (See ChemScan Application Summary # 96, Nitrification Process Control.)

Some treatment facilities do not have any capability to adjust the aeration rate in response to changes in demand. At these locations the amount of aeration supplied to the process was designed to always be in excess of the expected demand. This results in energy costs that are well in excess of the minimum required for treatment. Improper aeration can also have negative effects on sludge characteristics and on anaerobic and facultative processes such as denitrification and phosphorous removal. (See ChemScan Application Summaries #59, Denitrification Process Control and #94, Biological Nutrient Removal.) If improved treatment is required or if peak treatment demand at times exceeds the original design capacity, these plants may experience poor process performance during certain periods, poor energy performance during other periods and composite performance approaching or exceeding permit requirements.

Aeration control can be divided into two broad subjects: measurement of process variables to provide information for control adjustments and implementation of the aeration control adjustments.

Traditional Measurement Strategies

Feed Forward Control
If the objective is to adjust the aeration rate to match the requirements of the treatment process, some effort to measure or predict aeration demand may appear to be a reasonable approach. Such measurements may include flow rate, influent oxygen demand (ORP) and/or influent ammonia. These can all be classified as feed-forward control strategies. These strategies may not however, account for the many bio-chemical variables actually interacting within the process and therefore may not provide a satisfactory control signal for aeration rate adjustments.

Feed Back Control
Measurement of a process variable at or after the aeration adjustment location is a better approach. The measurement strategy can be based on regular grab samples or on automatic analysis. If grab samples are used, the frequency of analysis required for good control adjustment may be very labor intensive, especially if the measured parameters require physical or chemical analysis (such as alkalinity, COD or ammonia). If so, there is a temptation to reduce sample frequency and thus reduce the opportunities for process optimization and energy savings.

Feed back control strategies can also be based on automatic or continuous measurement of certain process parameters that tend to vary as aeration rates are altered. The most popular of these parameters is Dissolved Oxygen. Many operators believe that the objective of the treatment process is the creation of surplus dissolved oxygen in the effluent from the aeration basin. Actually, maintaining surplus oxygen in the effluent at an arbitrarily high set point is merely a convenient way to assure that the wastewater has been fully nitrified (all ammonia has been converted to oxidized nitrogen), which can occur only after a substantial reduction in carbonaceous demand has occurred. (See Figure 1) But this is at the expense of delivering more oxygen than is actually demanded by the process. The difference between the oxygen required too achieve process objectives and the oxygen delivered to meet a “target” set point represents a pool of energy savings that can be captured by using the appropriate measurements within the process. (ORP and alkalinity are two other measurements sometimes mentioned for control, but these parameters are indirect measurements at best and are also affected by chemistries and process conditions that are unrelated to those that would require aeration rate adjustments.)

If the objective of the process is nitrification, the most direct measurement strategy to maintain control at minimum energy cost is the measurement of ammonia in the process, certainly at the end of the aeration basin or in the aeration effluent but also at additional upstream sample points. A simple feed back loop can link changes in the aeration rate directly to changes in ammonia concentration. More aeration is provided when ammonia is high, less when little or no ammonia is present.

Profile Control

The most effective approach to achieve both process control and energy management objectives would be to monitor multiple points in the aeration basin, so that aeration rates can be adjusted at the earliest opportunity. This is especially true if aeration zones within the process can be independently controlled. Analysis of ammonia at multiple sample points across the process is called an “ammonia profile”.

Plants that have total nitrogen limits may also consider detection of additional parameters at strategic points within the process. Plants that perform both nitrification and denitrification should consider analysis of nitrite and nitrate in addition to ammonia. Analysis of nitrite is an early indication of process instability and analysis of nitrate shows the end result of nitrification (See ChemScan Application Summary #96, Nitrification Process Control and #59, Denitrification Process Control.) Detection of nitrite, nitrate and ammonia at strategic sample points across the process is called a “nitrogen profile”. The use of a nitrogen profile can help assure compliance with nitrogen removal requirements at a minimum cost for aeration, recirculation pumping and chemical addition. (Plants that perform chlorination may also benefit from analysis of a nitrogen profile, with possible savings from allowing controlled ammonia bleed for chloramine formation and additional savings from minimizing nitrite delivery to the chlorination process. (See ChemScan Application Summary #82, Wastewater Chloramination Process Control and #99, Chlorination Control.)

If phosphate is added to the profile, it is called a “nutrient profile”.

ChemScan Measurement Capability

ChemScan can provide systems for feed back control using on-line ammonia analysis. If the sample point is after the secondary clarifier, no filtration is required prior to analysis. If the sample point is in the aeration basin or prior to secondary settling, sample filtration will be required using either a cyclic filter (low volume, self purging, short distance) or a cross flow filter (high sample flush volume, long sample distances).

ChemScan can also provide central analysis systems capable of providing ammonia profile, nitrogen profile or nutrient profile measurements at multiple sample points across the process. A few (no more than 3) nearby sample points can use a central ChemScan analyzer with cyclic filters, while applications with several (up to 8) sample points typically use a central analyzer, cross flow filter and sample sequence controller in conjunction with either a central sample pump or individual sample pumps to obtain process profile measurements.

Implementation

Implementation of aeration control strategies will depend on the type of aeration systems in use at the plant and also on the capabilities these systems offer for control. Most control for mechanical aerators and blowers will involve the use of variable frequency drives. A variable frequency drive adjusts the speed of electric motors by modulating the power being delivered. Motor speed can thereby be matched to the amount of work demanded. Systems with variable frequency control can provide “soft start”, thus avoiding high torque, current surges and stress on the motor systems.

Control of diffused aeration systems will depend on blower type and strategy for coordination of multiple blowers. Blower types include constant speed centrifugal blowers, usually controlled by modulating air inlet valves or inlet guide vanes. Positive displacement (rotary lobe) blowers are controlled using a VFD to modulate the output.

Multiple blowers are coordinated by providing either parallel control (which simultaneously adjusts the output of all blowers following addition or deletion) or cascaded control (which adjusts the output of individual blowers to a minimum or maximum output before adding or deleting the next blower needed to satisfy the overall aeration demand).
​
Aeration control implementation often requires custom software based on the specific processes, control strategy, aeration systems and safety factors that apply to a specific treatment facility.

Aeration Control and Energy Cost Reduction, Copyright ChemScan, Inc.​
ChemScan, Inc.
2325 Parklawn Dr., Suite I, Waukesha, Wisconsin, USA 53186
​Phone: 262-717-9500
Toll Free: 800-665-7133
  • Applications
    • Municipal Water Monitoring >
      • Ammonia Feed
      • Chloramination Control
      • Chlorination
      • Color Analysis
      • Distribution Monitoring
      • Ion Exchange Breakthrough
      • Natural Organic Matter (NOM) Removal
      • Peak Point Chloramination Control
      • Phosphate Sequesterant Feed Control
      • Reservoir Monitoring
      • Security Monitoring
      • TOC Monitoring in Water
      • Well Blending
    • Wastewater Monitoring and Control >
      • Aeration Control and Energy Cost Reduction
      • Biological Nutrient Removal
      • Biological Phosphorus Removal
      • Chemical Phosphorus Removal
      • Chloramination /Breakpoint Avoidance
      • Chlorination/De-Chlorination
      • De-Nitrification Monitoring
      • Nitrification
      • Nutrient Deficiency Analysis
      • Lagoon Discharge
      • SBR Stage Control
      • TOC Monitoring
      • UV Disinfection Control
    • Industrial Water Treatment >
      • Boiler Water Analysis
      • Cooling Water Analysis (Closed Loop)
    • Industrial Process Monitoring >
      • Electroless Plating
    • ASA Technical Papers (ALL)
    • ChemScan Installation Photos
    • Success Stories
    • ChemScan Webinars
  • Service
    • Contact Service Request Form
    • ChemScan Service Team
    • MSDS
    • Communication Protocols
    • Software Utilities
    • Service Videos
  • Parts
  • Company
    • Terms and Conditions
    • Contact Form (General Inquiry)
    • Contact Service
    • Application Data Sheet
    • Employment Opportunities
    • ChemScan Representatives and Distributors
  • Products
    • ChemScan Mini Analyzer >
      • mini oP (Ortho Phosphate)
      • mini oP (Ortho Phosphate) Extended Range
      • mini Cu (Copper)
      • mini LoP (Low Ortho Phosphate)
      • mini UV-254
      • mini LowAm (Low Ammonia)
      • mini Mn (Manganese)
      • mini LowMn (Low Manganese)
      • mini LowChlor (Low Chlorine)
      • mini Sulfite
      • mini Ammonia
      • mini FreeAm (Free Ammonia)
      • mini Fe (Iron)
      • mini Ni (Nickel)
      • mini PAA (Peracetic Acid)
      • mini ChlorAm
    • ChemScan mini Accessories
    • ChemScan Process Analyzers >
      • ChemScan 2150/S Chloramination Analyzer
      • ChemScan 2150/DC Chem Feed Analyzer
      • ChemScan 2150/N Aeration Rate Analyzer
      • ChemScan 2150/NoP Chem Feed Analyzer
      • ChemScan 2150/NHoP Nutrient Analyzer
      • ChemScan 2150 Process Analyzer
      • ChemScan UV-3150 Process Analyzer
      • ChemScan 4100 Nutrient Control
      • ChemScan 6101 Nutrient Control
    • ChemScan Process Analyzers with HMI >
      • ChemScan 2250/S HMI Chloramination Analyzer
      • ChemScan 4200 HMI Analyzer
      • ChemScan 3250 HMI Analyzer
      • ChemScan 2250/NoP HMI Analyzer
      • ChemScan 2250/NHoP HMI Analyzer
      • ChemScan 2250/N HMI Analyzer
      • ChemScan 2250 HMI Analyzer
      • ChemScan 6201 HMI Analyzer
    • ChemScan Analyzer Accessories
    • ChemScan Sensor Family