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Technical Description <br /> Floating solids which surface during the clarification cycle are not lost during normal operation, <br /> but are returned to the mixed liquor each sludge-return cycle in the following manner: <br /> The supernatant is pumped out of the clarifier except for the top three inches that remain on the <br /> surface of the sludge volume. The entire sludge volume, except that which cannot reach the vo- <br /> lute of the return pump, is returned to the aeration chamber by the sludge return pump. The re- <br /> maining sludge and floatables. now settled on the tank bottom, are weired back to the aeration <br /> chamber during the MLT pump overrun on the next batch cycle. <br /> After settling has occurred, the microprocessor initiates the supernatant transfer pump (SNT), <br /> which transfers the supernatant into the chlorine contact chamber. During the supernatant transit, <br /> ozone is injected into a distribution manifold in the bottom of the ozone contact chamber. Ozone <br /> injection continues for 40 minutes after the chamber is filled. <br /> NOTE. Following are the reasons we do not recommend the use of chlorine as a disinfec- <br /> tant. Some states are currently passing legislation preventing the use of chlorine as a disinfectant <br /> in both wastewater and freshwater applications. This is done for reasons of health for both the <br /> environment and living creatures. A simplified explanation of the reasoning follows: <br /> In order to ensure that enough chlorine has been applied to achieve a maximum pathogen kill, <br /> there must be a measurable amount of chlorine in the system discharge. In the case of water- <br /> body discharge, this small amount is deadly to virtually all-natural life forms in the water. In the <br /> case of land-surface discharge, over a period of time chlorine will build up to a level high enough <br /> to cause conversion of soil-bound minerals to salts, which are not only toxic to the soil but will <br /> leach out into groundwater supplies. These conversions are expressed as: <br /> Cl -r Na NaCl <br /> Cl+K KCl <br /> Cl+ Mg MgC12 <br /> Cl +Ca — CaCl2 <br /> In addition, the factors that affect the bacterial and virucidal efficiency of chlorine can vary <br /> widely on a seasonal basis from day to day and from daytime to nighttime. In fact,marked varia- <br /> tions have been shown in samples taken from the same effluent stream at intervals as short as one <br /> hour. <br /> The source of chlorine may take many forms. The important thing to remember is that chlorine <br /> derived from almost any source forms hypochlorous acid in dilute solutions used for wastewater <br /> disinfection. Hypochlorous acid is an extremely potent germicide at pH levels between 6.5 and <br /> 7.5, which covers most wastewater applications. However, it is also a highly active oxidizing <br /> agent and is therefore short-lived as it reacts with ammonia to form chloramines as: <br /> NH3+HOCI NrH.Cl (monochloramine)-+ H2O <br /> NH 20 +HOCI NHC, (dichloramine)+H2O <br /> NHCI 2+HOCI —► NC13 (nitrogen trichloride)+ H2O <br /> These reactions are extremely important, as the disinfecting power of a unit of chlorine as hy- <br /> pochlorous acid is between 25 to 100 times as great as that of a unit of chlorine as <br /> monochloramine. If the effluent has not gone through a quality nitrification/denitrification proc- <br /> -7 <br /> 7•H Technical Services Group, Ina <br /> I <br />