ii

ii. Constructed to withstand the earth pressures encountered and able to withstand the chemical effects of chlorine and wastewater. iii. Equipped with baffles or provided with an inlet to provide adequate mixing and contact of chlorine and effluent. The inlet and outlet must be Schedule 40 PVC pipe, 4 inches in diameter with the outlet tee extending 6 inches from the bottom of the chamber. [See Figure 30.] iv. Designed and located to have access a minimum of 6 inches above final grade. v. Provide 65 gallons (minimum) capacity or 1 hour retention. NOTE: If the chlorine contact chamber is an integral component part of the design of the Advanced Treatment System the efficiency shall be certified by the third- party certifying entity. vi. Sealed (water-tight) to prevent the entry of surface or ground water. It is recommended that the outlet be placed above any seasonal water tables as indicated by gray mottles. An approved sealant shall be applied to the lid, inlet, outlet and access opening to prevent groundwater and surface water intrusion. vii. Consideration will be given to 2 flow-through units with common-wall construction so that each side satisfies the detention requirements. The chlorine feed rate will be proportioned in accordance with the flow and the chlorine demand of the wastewater. Adequate mixing during the chlorine contact period will be insured by the installation of adequate baffling. viii. Pumped periodically for sludge accumulation and properly disposed. b. The feeder tube and liquid chlorinator dosing compartment must meet the following requirements: i. Installed level on undisturbed earth or backfilled with sand. ii. Charged with a minimum of 3 calcium hypochlorite chlorine tablets or the dosing compartment is ½ filled with liquid chlorine. iii. Equipped with a method for removal. The method of removal must be within 3 inches of the chlorinator opening. iv. Constructed of Schedule 40 PVC pipe, 3 inches in diameter and provide removal of all chlorine tablets when feeder tube is removed from chlorinator. [See Figure 31.] v. Childproof and tamper resistant, or limited access cover. 2. Ultra-violet: a. The main components of an ultra-violet disinfection system are mercury arc lamps, a reactor, and ballasts. The source of the ultra-violet radiation is either the low-pressure or medium-pressure mercury arc lamp with low or high intensities. b. The optimum wavelength to effectively inactivate microorganisms is in the range of 250 to 270 nm. Low-pressure lamps emit essentially monochromatic light at a wavelength of 253.7 nm. Standard lengths with diameter of 1.5–2.0 cm. The ideal lamp wall temperature is between 95 and 122ºF. c. The effectiveness of an ultra-violet disinfection system depends on the characteristics of the wastewater, the intensity of the ultra-violet radiation, the amount of time the microorganisms are exposed to the radiation, and the reactor configuration. d. All ultra-violet disinfection must provide a flow either parallel or perpendicular to the lamps and have a ballast or control box which provides a starting voltage for the lamps and maintains a continuous current. e. There are two types of ultra-violet disinfection reactor configurations that exist: i. Contact: This reactor contains a series of mercury lamps enclosed in quartz sleeves to minimize the cooling effects of the wastewater. The lamps are placed parallel or perpendicular to the direction of the wastewater flow. Flap gates or weirs are used to control the level of the wastewater. ii. Noncontact: This reactor contains mercury lamps suspended outside the transparent conduit, which carries the wastewater to be disinfected. f. The ultra-violet disinfection must provide the following: i. Necessary hydraulic properties for maximum exposure to ultra-violet radiation. ii. Necessary intensity of ultra-violet radiation needed for effective inactivation of microorganisms. iii. Necessary radiation for peak flow condition, suspended or colloidal solids, initial bacterial density and any other physical and chemical parameters (i.e., hardness, iron, pH or TSS). g. The ultra-violet disinfection system must ensure that sufficient radiation is transmitted to the organisms to render them sterile. All surfaces between the radiation and target organisms must be clean, and the ballast, lamps, and reactors must be functioning at peak efficiency. h. The sleeves or tubes must be cleaned regularly by mechanical wipers, ultrasonics, or chemicals. The cleaning frequency is dependent upon the wastewater characteristics produced by the Advanced Treatment System. i. The retention time for complete inactivation will be determined by size of reactor and lamp intensity. j. All disinfection systems certified by American National Standards Institute/National Sanitation Foundation International Standard 46 will be accepted for registration in Mississippi provided documentation is submitted with application. k. All disinfection systems not certified by American National Standards Institute/National Sanitation Foundation International Standard 46 must submit all documentation to determine compliance with Rules 6.1.3 through 6.1.7. 3. Ozone: a. These products will be reviewed by the Division in accordance with design, construction and installation for the specific location and usage. b. These products will only be approved by the Division after certification by a Professional Engineer registered in the State of Mississippi after having shown it can be constructed and installed by the Certified Installer. c. This product will require that the Professional Engineer train and certify the Maintenance Provider in its routine operation and maintenance, as well as safety guidelines.