Liquid Phase Collection System Odor Control 101

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Transcription:

Liquid Phase Collection System Odor Control 101 Presented by Richard Finger

Presentation Outline General System Considerations Treatment Technologies Air and Pure Oxygen Injection Oxidants Chlorine and Hypochlorite Hydrogen Peroxide Ozone Iron Salts

Presentation Outline (Cont.) Treatment Technologies (cont.) Caustic Dosing Continuous Shock Dosing Nitrate Salts Anthraquinone Enzymes and Bacterial Augmentation Summary

General System Considerations Think System Wide There may be people working in the collection system downstream of chemical addition Chemical doses (and their effects) end up at the treatment plant Evaluate cost-effectiveness based on actual performance at your site Conduct thorough monitoring to evaluate performance of chemicals

Air and Pure Oxygen Injection Direct Injection to Forcemains Injection into High Pressure Side Streams or Inverted Siphons for Gravity Systems Introduction of Oxygen can: Inhibit the growth of sulfate reducing bacteria Chemically oxidize sulfide Promote biological oxidation of sulfide

Air and Pure Oxygen Injection (Cont) Air Injection Need to Consider Forcemain Profile Need to Consider Forcemain Composition Best for Pressure Systems (forcemains) Need to Know Oxygen Uptake Rate (4-20 mg/l/hr) Effective Treatment Duration is a Function of Uptake Rate. Most Effective at Inhibiting Sulfide Generation Can be Relatively Inexpensive

Air and Pure Oxygen Injection (Cont) Pure Oxygen Injection Can Dissolve 5X More Oxygen Than with Air Does Not Introduce Nitrogen, Thus Less Potential for Gas Accumulation at High Points Can Usually Lease Storage/Vaporization Equipment. Will Need Booster Blower at Pressures > 40 psi

Oxidants Chlorine and Hypochlorite Chlorine is Being Phased Out in Favor of Hypochlorite Mixes Rapidly with Wastewater Rapidly Reacts with Inorganics (<1 min) Dosage Rate in Range of 8 lb Chlorine per lb Sulfide Treatment Effective for About 4 Hours Reasonably Simple to Implement

Hydrogen Peroxide Oxidants (Cont) Oxidizes Sulfide to Sulfate and Sulfur Dosage in the Range of 4-8 pounds H 2 O 2 per Pound Sulfide Requires 15-30 Minutes for Complete Reaction Can Also Serve as a Source of Oxygen to Inhibit Sulfate Reduction. Requires Special Equipment, Which Can Be Leased from Vendor Provides About 4 Hours Control

Hydrogen Peroxide Storage

Ozone Oxidants (Cont) Most Often Used in Pump Stations to Treat Air Strong Oxidant, Which is Not Selective for Sulfide Normally Too Expensive for Liquid Stream Treatment

Iron Salts Includes Ferrous/Ferric Chloride and Ferrous Sulfate Sulfide is Removed by Precipitation with the Iron Dosage is not Stoichiometric and Varies as a Function of the Level of Control Required Dosage in the Range of 1.5 2 Pounds Iron per Pound Sulfide with Limit of ~0.5 mg/l S Organic Acids Can Interfere with Reaction Can Also Help Control Sulfides in Digesters Can be Cost Effective Are Classified as Hazardous Chemicals

Ferric Chloride

Caustic Dosing Availability of Hydrogen Sulfide for Release to the Atmosphere is a Function of ph

Effect of ph on Hydrogen Sulfide -Sulfide Equilibrium Percent of Total 100 90 80 70 60 50 40 30 20 10 0 Hydrogen sulfide-sulfide Equilibrium H2S HS - This Stinks! These do not. HS -2 4 5 6 7 8 9 10 11 12 13 14 ph H2S HS- S=

Caustic Dosing (cont) Available Chemicals include Sodium Hydroxide (25 and 50%) Lime Magnesium Oxide/Hydroxide Sodium Hydroxide is Most Commonly Used Classified as a Hazardous Chemical, so Significant Storage/Handling Issues If Stored On-site, Need Heat Tracing

Caustic Dosing (cont) Continuous Dosing Raising ph to Between 8 and 9 Prevents Available Sulfide from Being Released to Atmosphere Can Require a Significant Quantity of Caustic Over Time Dosage Rate is Unrelated to Sulfide Concentration, but Depends on Wastewater Alkalinity Not Commonly Used Because of Cost and Potential Treatment Plant Impacts

Slug Dosing Caustic Dosing (cont) Goal is to Raise ph to 12.5 or Above for at Least 20 Minutes Inhibits Sulfide Generation by Stripping Slime Layer Effect Lasts from 4 Days to Several Weeks, so Requires Periodic Dosing During the Odor Season Works on Both Forcemains and Gravity Sewers

Caustic Dosing (cont) Slug Dosing (cont) Dosage is Dependent on the Wastewater Alkalinity Significant Risk to Collection System Personnel and Downstream Facilities Best Used On Sub-systems with Flows Not Exceeding 10% of Total System Flow Dosing Can be Done Using Tank Truck, Thus Avoiding Fixed Facilities Can Be Cost Effective in Some Applications

Caustic Storage Tank

Nitrate Salts Most Common Sources are Calcium and Sodium Nitrate. May be Considered Proprietary Products Serve as an Oxygen Source, so Can Both Inhibit Sulfide Generation and Oxidize Existing Sulfide Generally Require a Period of Dosing to Achieve Full Effect Dosage Varies Based on Several Factor, so Needs to be Adjusted Based on System Monitoring

Nitrate Salts (cont) Dosages in the Range of 1-3 Pounds Nitrate Oxygen per Pound of Sulfide are Common Proprietary Combinations are Available That Combine Nitrate Salts with Caustic or Other Chemicals That Inhibit Sulfate Reduction or Sulfide Release Products are Not Classified as Hazardous Can Often Be a Cost Effective Solution Avoid Calcium Nitrate When Waste Stream Contains High FOG Concentrations

Nitrate Feed System

Nitrate Feed System

Anthriquinone Inhibits the Ability of Organisms to Reduce Sulfate Requires Periodic Dosing as Effect Wears Off Has Not Worked in Some Applications Available in Combination with Nitrate Products (Proprietary Product) Cost Effectiveness Needs to be Evaluated On-site

Enzymes and Bacterial Augmentation Focus is on Changing the System Ecology Limited Data on Effectiveness

Discussion Many Technologies/Approaches Available Applications are Often Site Specific Due to Both System Characteristics and Local Chemical Price Variability Systems Should Be Tested Prior To Implementation Systems Should Be Re-evaluated Periodically Spend 1% to 10% of Annual Chemical Cost Tracking Performance

Discussion Evaluation Criteria For Choosing an Odor Control Method Characteristics of the wastewater Type of odor being controlled Cost Effectiveness Safety Regulatory compliance Operability Maintainability Environmental issues Site space available Aesthetics