For example, Iron is most commonly found in its soluble state as ferrous bicarbonate, Fe (HCO3)2. Ferrous iron has a positive two valence. As ferrous iron is oxidized, the number of electrons is reduced and the iron develops a valence of positive three, ferric hydroxide, Fe (OH)3.To fully aerate iron, the amount of dissolved oxygen present must be at least 15% of the total amount of iron present. When dissolved oxygen is sufficiently present, the iron and oxygen bond together. Soluble ferrous bicarbonate may be completely oxidized and changed to the insoluble ferric hydroxide precipitate, Fe (OH) 3, except when the water is acidic. The insoluble ferric hydroxide is commonly described as red water. When iron is fully oxidized in alkaline water, iron readily precipitates.
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Oxidation is the loss of electrons from the reducing agent. Since electrons carry negative charges, oxidation results in an increase of positive valence. Oxidation reduces the number of electrons orbiting an element causing the element to bond with oxygen, which has attraction for those electrons. Hence, oxidation/reduction.
One of the requirements for successful precipitation is to provide sufficient contact time for the oxygen and minerals to react. For iron removal, it is generally best to have an aeration tank, which provides contact time and a vent to expel excess air. That tank should be about the same size as the filter tank(s). Well-designed aeration tanks are constructed so that a pocket of air is maintained at the upper one-third to one-half portion of the tank height. An inlet diffuser allows the water to spray in the pocket of air. Depending upon the chemical properties of water, a 10x54 aeration tank works well for iron and hydrogen sulfide, (H2S), on most residential applications. H2S levels in excess of 10 mg/l will require larger aeration tanks.
Precipitated iron is filtered successfully with a variety of filter media. It may be necessary to experiment to determine which filter media works best in that area. Dealers can avoid future service problems by initially sizing the filtering system properly. The flow rate of the water at the pressure tank should be measured accurately because many filter media require approximately twice the backwash flow rate as the service flow rate.
Timing how long it takes to fill up a measured bucket is an inaccurate method of attaining flow rates. The proper well water flow rate is determined by counting the gallons drawn down and the time between cut in and cut off cycle of the well pump. To do this, one must allow the well pump to build up to full pressure. Close the main shut off valve to the building. Measure the number of gallons drawn down from the pressure tank until the well pump turns on. Time the period it takes for the well pump to recover, that is, between cut in and cut out. The formula for determining the flow rate is gallons drawn down that were measured above, divided by the seconds required for recovery, then multiply by 60.
Considering that the backwash rate for many filter media should be twice the filter rate, it may be necessary to install a second filter in parallel to accommodate the service flow. In the illustration above where eight gallons is determined as the flow, that flow will be adequate to backwash many filter media in an eight to ten inch diameter tank. However, the service flow for many common filter media in eight to ten inch diameter tanks is about four or five gallons per minute. Hence, forcing eight gallons per minute through a single ten-inch tank may pass iron. In order to govern the flow of water evenly through tanks installed in parallel, flow restrictors may be installed on the outlet side of the filter tanks.
For example, if 8 gallons are drawn down and it takes 60 seconds to build pressure back up, then: 8 divided by 60 = .133. Consequently, .133 × 60 = 8 gallons per minute flow rate.
Pictured above is an oxidation ditch during the anoxic stage of the aeration process during wastewater treatment.
Aeration or the addition of oxygen is one of the most critical and energy-intensive processes in wastewater treatment, consuming up to 50 to 60% of the overall energy required by a wastewater treatment plant (WWTP). Aeration produces dissolved oxygen (DO) to facilitate the growth of microorganisms and is used across all stages of wastewater treatment.
Finding the optimal amount of aeration directly affects wastewater treatment efficiency. Lower aeration inhibits the nitrification reaction in the system, resulting in low DO concentration and continually expanding sludge in the aeration tank. A greater aeration volume leads to higher DO concentration and increased air agitation and sedimentation of suspended solids. As the wastewater quality declines, treatment costs increase because of higher energy consumption.
Below, we discuss the aeration process in wastewater treatment through primary, secondary and tertiary stages and why you need to partner with a team of experienced wastewater engineers to determine the proper aeration system for your local publicly owned treatment works (POTW).
Aeration process in wastewater treatment
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Surface aerators like those in this picture facilitate aeration in a lagoon WWTP system.
In wastewater treatment, the aeration process brings water and air into close contact to oxidize dissolved metals and remove dissolved gases and volatile organic compounds. Aeration improves effluent quality during the following steps in the treatment process:
Based on the treatment stage, effluent quality and the capacity of a treatment plant, the most common types of aeration systems used in POTWs are:
Optimizing the energy consumption of aeration systems is a priority for WWTP operators. The mixers in aeration systems keep biosolids suspended once the desired oxygen level has been achieved in aeration tanks or digesters. This saves significant amounts of energy during additional mixing.
Some communities with smaller populations use lagoon systems for wastewater treatment, using variable frequency drives and DO meters to adjust the aeration process and lower utility bills. Determining the right aeration system to help lower your treatment plant's energy bills while addressing the effluent demand requires expert guidance from a team of wastewater engineers.
Partnering with a wastewater engineer to select the right aeration system
At Fehr Graham, we understand the challenges municipalities face in designing aeration systems to treat wastewater per local effluent standards while optimizing energy consumption. From evaluating, planning and designing solutions to improve the efficiency of your community's POTW to helping you secure funding solutions for construction and upgrades, we can guide you to the best choices for effective and energy-efficient wastewater treatment operations.
To learn more about how Fehr Graham can help improve the aeration process in wastewater treatment at your local POTW, contact us or give us a call at 815.235..
Edgar Mendoza is a Water and Wastewater Operations Specialist. He specializes in process control of wastewater and water treatment facilities, wastewater collection sewer systems, pump stations, water distribution and storage systems. Contact him atThis address is being protected from spambots. You need JavaScript enabled to view it.
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