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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.

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Presentation on theme: "Ammonia Analyzer Provides Real Time Process Control Capability PWO Operator Seminar – February 22, 2002 Greg Farmer - Littleton / Englewood WWTP Gary Girolimon."— Presentation transcript:

1 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

2 Littleton / Englewood WWTP Process Schematic

3 Before Automating Process Control Diurnal ammonia variations led to:  Breakpoint chlorination  Inconsistent fecal coliform counts

4 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

5 Ammonia Control

6 Nitrifying Trickle Filters

7 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.

8 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.

9 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 >

10 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.

11 Pump Speed Control Operation By-pass valve Position > < NTF Pump Output Nitrate > < Ammonia

12 Chlorination

13 Controlled Chlorine to Ammonia Ratio

14 Fecal Coliform Counts

15 Analyzer Accuracy

16 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.

17 Final Effluent Ammonia vs. STIP Daily Average

18 Nitrate Buoy Recalibrated During Regular Maintenance - Suspect Poor Quality 3 rd party Reagent

19 ISCO/STIP Process Buoy

20 STIP Process Buoy  Operates by being placed directly in wastewater (even activated sludge)  Separate buoys for ammonium and nitrate

21 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

22 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

23 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

24 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

25 Method of Analysis - Schematic

26 Calibration  Buoy calibration is done using three step standard addition method  Calibrated automatically once per day

27 Buoy Bulkhead Layout

28 Process Buoy In Open Position  Shows Settling Chamber Settling Chamber Measuring Chamber Measuring Chamber Electrodes Electrodes Valves Valves Amplifiers Amplifiers

29 Process Buoy Without Stainless Steel Housing

30 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

31 The End


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