-•••Jt;i' --— ------- WHAT IS OXYGEN AERATION? One common, or conventional, method of treating wastewater is the activated sludge process. This process—as all bio- logical treatment processes—functions by contacting wastewater with bacteria able to break down organic material and there- by reduce the amount of pollutants in the wastewater. The bacteria utilized in the activated sludge process to perform this operation are contained in the material settled out of a wastewater stream after oxygen is introduced into the system. This mass of settled solids, called activated sludge, is then mixed with the wastewater being treated. Introduction of oxygen in- to the system, and mixing of the activated sludge with the wastewater both occur in the same tank, as can be seen from the accompanying schematic diagram. Historically, this required oxygen has been provided by the introduction of atmos- pheric air into the treatment system. Oxygen gas, however, possesses certain characteristics which can make its use, in lieu of atmospheric air, advantageous. One of these is the high partial pressure of pure oxygen. Since air contains only a- bout 21 percent oxygen, the use of pure oxygen instead of air in that portion of the treatment system needing oxygen in- creases the oxygenation capacity by a fac- tor of nearly five. As a result, smaller aeration tanks can be used to treat the same amount of wastewater. This utiliza- tion of pure oxygen rather than atmos- pheric air to provide the oxygen required in treating sewage is oxygen aeration. WHAT ARE THE APPLICATIONS OF OXYGEN AERATION? Oxygen aeration can be used for the con- struction of new facilities and for up- grading the capacity and performance of existing overloaded secondary treatment facilities. Several applications include: 1. Upgrading of existing overloaded ac- tivated sludge plants by conversion from air aeration to oxygen aeration. 2. Upgrading of existing trickling filter plants by adding oxygen aeration as a second stage biological step in the treatment system. 3. New plant construction, both with and without primary sedimentation. ------- FINAL CLARIFIER SCHEMATIC DIAGRAM OF MULTI-STAGE OXYGENATION SYSTEM WHAT ARE THE ADVANTAGES OF OXYGEN AERATION? Potential benefits, depending on the spe- cific installation and application, include: 1. Improved reliability of treatment per- formance 2. Reduced waste sludge production 3. Increased plant organic loading ca- pacity 4. Improved resistance to toxic sub- stances 5. More effective odor control 6. Reduced power requirements Higher dissolved oxygen the treated effluent content in Generally speaking, there is also an eco- nomic advantage over conventional aera- tion methods for plants with capacities greater than 5 million gallons a day. In the smaller capacity plants, the major ad- vantages involve greater acceptance of un- usually strong loads and greater treatment process reliability. WHAT'S INVOLVED? This schematic diagram depicts the equip- ment involved and operation of a typical multi-stage oxygenation system. Basic dif- ferences between this system and a con- ventional air aeration system are the tank covers and compressor units. High purity oxygen (90-100%) enters the first stage of the system and flows concur- rently with the wastewater being treated through the oxygenation basin. Pressure under the tank covers is essentially atmos- pheric and sufficient to maintain control and prevent back mixing from stage to stage. This allows for efficient oxygen uti- lization at low power requirements. Mix- ing within each stage can be accomplished either with surface aerators or with a sub- merged rotating sparge system (shown). The selection of the number of stages and the type of mixing device are variables that depend on waste characteristics, plant size, land availability, treatment require- ments and other similar considerations. HOW MUCH DOES IT COST? The chart below depicts representative total treatment cost ranges for oxygen aeration activated sludge plants. The costs shown are for construction of new treat- ment facilities and include operation, maintenance and capital amortization (5l/2%-25 years) costs for primary treat- ment, secondary treatment, and sludge handling and disposal facilities. ACTIVATED SLUDGE WASTEWATER TREATMENT PROCESS PRIMARY CLARIFICATION FINAL CLARIFICATION AERATION PRETREATMENT DISINFECTION ------- A new wastewater treatment process has been developed which utilizes oxygen-en- riched air or pure oxygen. This process is termed oxygen aeration or, more simply, oxygenation. The potential of oxygen aer- ation has resulted in an extremely rapid acceptance by consulting engineers, mu- nicipalities, and industries. The first full- scale application of the oxygen aeration process to the treatment of municipal wastewater occurred in 1969 under a dem- onstration contract from the U.S. Environ- mental Protection Agency's forerunner, the Federal Water Pollution Control Ad- ministration. In this demonstration pro- ject, a total of 1.25 million gallons per day of sewage was treated. Today, just three years later, over 35 full-scale muni- cipal wastewater treatment plants which will utilize the oxygen aeration process are in various stages of design and con- struction. The total amount of sewage to be treated by these plants exceeds 1.5 bil- lion gallons a day. ------- 13EZ ^.^^^^^^^^ \ WHO IS USING OXYGEN AERATION? Below is a partial listing of full-scale mu- nicipal wastewater treatment plants cur- rently using or planning to use oxygen aeration. „- Size (Million Location Gallons/Day) Detroit, Michigan 300 Middlesex County, N.J. 120 East Bay MUD. Calif. 120 Louisville. Ky. 105 Miami. Fla. 55 Hollywood, Fla. 36 Danville. Va. 24 Euclid. Ohio 22 Newtown Creek, N.Y.C. 20 Decatur, 111. 18 Fayetteville. N.C. 16 Salem, Oregon 16 New Rochelle, N.Y. 14 Fairfax County, Va. 1 2 Jacksonville, Fla. 10 Speedway.Ind. 10 Morganton, N.C. 8 Deer Park, Texas 6 Baltimore, Md. 5 WHERE CAN I GET MORE INFORMATION? Contact your consulting engineering firm or write to: Technology Transfer Environmental Protection Agency Washington, D.C. 20460 ft CPO ; 1973 O - 496-696 ------- |