Session 11 3

Information about Session 11 3

Published on August 22, 2007

Author: Woodwork

Source: authorstream.com

Content

Using the CPE Approach to Optimize Industrial Waste Treatment Facilities:  Using the CPE Approach to Optimize Industrial Waste Treatment Facilities Ronald G. Schuyler and Michael Rothberg Rothberg, Tamburini, and Winsor, Inc. Denver, CO And Deb Skirvin, Steve Hamilton and Kelly Peters Hercules Incorporated, Louisiana, MO RTW Coauthors:  Coauthors Mike Rothberg, RTW Deb Skirvin, Hercules Steve Hamilton, Hercules Kelly Peters, Hercules Comprehensive Performance Evaluation:  Comprehensive Performance Evaluation CPE - Evaluation Phase Design, administration, operation, maintenance Assess capability of major unit processes Identify performance limiting factors CCP - Composite Correction Program phase Systematic approach Eliminate factors inhibiting performance * *Hegg, DeMers and Barber CPE Process:  CPE Process Originally designed for municipal facilities Evaluation approach Major unit process criteria Administration, design, operation, maintenance factors Approach applied to industrial facilities Revised loading criteria Same biological, chemical and physical laws Apply them to minimize poor performance Procedure:  Procedure Become familiar with existing facility Define present plant loadings Define major unit process characteristics Define present operating conditions Suggest process control modifications Suggest simple process modifications Identify longer-term oriented modifications Communications:  Communications Operation/consultant staffs side-by-side Lab Control room On/in the tanks 3-4 days Listen to operating staff experience Compare to accepted standards Verify validity or suggest alternate finding Missouri Chemical Works:  Missouri Chemical Works 1996 Conditions:  1996 Conditions Flow = 0.32 MGD Influent BOD = 11,190 lb/day (about 4,193 mg/L) COD = 23,915 lb/day (about 8,961 mg/L) Effluent BOD = 77 lb/day (about 29 mg/L) COD = 1,271 lb/day TSS = 50 lb/day (about 19 mg/L) 1996 Process Data:  1996 Process Data MLSS/MLVSS = 6,305/5,376 mg/L (85% vol) RAS flow = 0.504 MGD, 160% of influent WAS = 1,460 lb/day MCRT = 73 days F/M andlt; 0.1 lb/lb Polymer added = 283 lb/day (1995/96 Ave.) Antifoam added = 54 gal/mo (1995-96 Ave.) PE Lake:  PE Lake Flow equalization Load equalization Toxic materials such as formaldehyde Slowly degradable formaldehyde derivatives Storm water Some volatilization of organics EQ Basin:  EQ Basin Maintained at 10-10.5’ depth Load equalization About 7 days DT Received no return sludge Aerated to control odors 25% COD removal without biomass return No temperature control Aeration Tank:  Aeration Tank 20’ deep Parkson Biolac aeration chains 2.4 days detention time @ Q = 0.5 MGD and RSF = 0.5 MGD MLSS about 6,000 mg/L Maintain temperature about 95°F (35°C) Volumetric loading = 32-52 lb BOD/103 ft3 Secondary Clarifiers:  Secondary Clarifiers 2-45’ diameter, 12’ deep 101 gal/ft2/day, 13.6 lb MLSS/ft2/day Return ratio Average = 160% Peak month = 312% Blanket thickness about 1-2 feet Periodic 'black' layer required high RSF Polymer addition Average = 283 lb/day Peak month = 620 lb/day Process Modifications:  Process Modifications Convert EQ basin to aeration tank Reduce MLSS in both tanks to about 3,700 mg/L Reduce return rate to less than 100% of Q Take one secondary clarifier off line Reduce variability of organic loading Convert EQ Basin to Aeration Tank:  Convert EQ Basin to Aeration Tank Bring some return sludge to EQ Low temperature = lower metabolism rate Increase aeration to maintain DO about 2 mg/L Aeration capacity?? Could only use one 600 hp blower? Not enough! Two blowers would 'kick-out' both blowers Calculations did not verify this Started both andlt; 70% Plenty of air Reduced volumetric loading and F/M Reduce MLSS:  Reduce MLSS Maintain about 3,750 mg/L Increase total biomass by 50% Use EQ basin Addresses organic/toxic/foaming shocks Reduce polymer dose Reduce Return Sludge Flow Rate:  Reduce Return Sludge Flow Rate Reduced total flow to clarifiers Reduce polymer poundage at same dose Reduce solids load to clarifier Remove One Secondary Clarifier:  Remove One Secondary Clarifier Not required with lower solids loading Not required with less total flow (Q + RSF) Largest problem was with operations staff Always needed two clarifiers to settle sludge Never operated with just one Trial OK Half-hour blanket readings Back to two clarifiers if blanket rises over a foot Raised 6' in first half-hour Back to 1-2 feet thickness within one hour Have not used two clarifiers together since then Stabilization of Organic Loading:  Stabilization of Organic Loading Long-term Work with production staff Reduce unusual discharges Notify operations when problem occurs Environmental and Production groups are now a team! Results:  Results Effluent quality improved Organic loads stabilized Secondary clarifier blankets maintained at normal Chemicals saved Polymer Antifoam Significant monetary savings Effluent Quality:  Effluent Quality Organic Load Stabilization:  Organic Load Stabilization Polymer and Antifoam Use:  Polymer and Antifoam Use Summary:  Summary Initiated CPE Made simple process changes Reduced polymer use by average 66% Eliminated use of antifoam Reduced effluent BOD and TSS Reduced influent organic load Reduced costs significantly Great communications and teamwork

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