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Ammonia Analyzer Provides Real Time Process Control Capability PWO Operator Seminar – February 22, 2002 Greg Farmer - Littleton / Englewood WWTP Gary Girolimon - Ted Miller and Associates
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Littleton / Englewood WWTP Process Schematic
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Before Automating Process Control Diurnal ammonia variations led to: Breakpoint chlorination Inconsistent fecal coliform counts
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Benefits Dial in Final Effluent Ammonia Concentration Centrate Return Timing Feedback Maximize Nitrifying Trickling Filter (NTF) Efficiency More Consistent Fecal Coliform Counts Through Control of Ammonia to Chlorine Ratio Only 2-3 hours/month Maintenance
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Ammonia Control
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Nitrifying Trickle Filters
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NTF Effluent Ammonia Control Modes By-Pass Valve Control 24 / 7 Effluent ammonia goal is 2.0 mg/l Valve opens incrementally when ammonia is below 2.0 mg/l Valve closes incrementally when ammonia above 2.0 mg/l Pump Control If ammonia level increases above 7.0 mg/l, NTF pump speeds increase When ammonia falls below 5.0 mg/l pump speeds decrease. Pumps cannot go below a preset speed so that the minimum hydraulic loading is maintained.
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By-Pass Valve Control If the analyzer detects ammonia level below the set point, the by- pass valve opens incrementally. If the analyzer detects ammonia levels above the set point, the by-pass valve closes incrementally.
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By-Pass Valve Operation Ammonia > Valve closes when ammonia level increases above set point of 2 mg/l. Valve opens when ammonia level decreases below set point of 2 mg/l. < Valve position Nitrate >
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Pump Speed Control If the analyzer detects ammonia levels below a set point the NTF pumps speeds decrease. Pump speed cannot go below a selected value so that the minimum hydraulic loading is maintained. If the analyzer detects ammonia levels above a set point the NTF pump speeds increase.
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Pump Speed Control Operation By-pass valve Position > < NTF Pump Output Nitrate > < Ammonia
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Chlorination
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Controlled Chlorine to Ammonia Ratio
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Fecal Coliform Counts
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Analyzer Accuracy
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Instrument Accuracy Analyzer vs. Lab Instrument values are extracted daily at 8:00 am and logged to the historical data server. Operators collect a sample near the analyzer at ~8:00 am for analysis by the lab.
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Final Effluent Ammonia vs. STIP Daily Average
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Nitrate Buoy Recalibrated During Regular Maintenance - Suspect Poor Quality 3 rd party Reagent
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ISCO/STIP Process Buoy
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STIP Process Buoy Operates by being placed directly in wastewater (even activated sludge) Separate buoys for ammonium and nitrate
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STIP Process Buoy Follows EPA approved methods of analysis Operates in a batch analysis mode with typical analysis times of 3 to 5 minutes Measuring range of 0.1 - 50 mg/l as N for both nitrate and ammonium
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Method of Analysis - General Solenoid valve opens permitting sample to fill settling chamber via hydrostatic pressure Sludge settles for pre programmed time period Ammonium and nitrate measured with ion selective electrodes (ISE) Solenoid valve reopens permitting supernatant to fill measurement chamber
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Method of Analysis - NH 4 N Caustic (NaOH) added till pH>11.5 Ammonium is converted to Ammonia (gas) Ammonia measurement taken with gas selective electrode
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Method of Analysis - NO 3 N Conductivity sensor used to add reagent (ion suppression) to adjust ionic strength of solution Concentration measured with nitrate selective electrode
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Method of Analysis - Schematic
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Calibration Buoy calibration is done using three step standard addition method Calibrated automatically once per day
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Buoy Bulkhead Layout
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Process Buoy In Open Position Shows Settling Chamber Settling Chamber Measuring Chamber Measuring Chamber Electrodes Electrodes Valves Valves Amplifiers Amplifiers
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Process Buoy Without Stainless Steel Housing
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Controller One controller can operate two buoys LCD screen displays current reading and graph of last 6- hours of operation Outputs: 4-20 mA 4-20 mA Bi-directional RS 232 Bi-directional RS 232
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The End
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