Laserfiche WebLink
Design parameters for the proposed mound system can be found in Appendix G. <br /> Design of the mound system for the Temple is based upon operating parameters, specifically <br /> wastewater flows, longevity, and environmental protection. If plumbing fixtures do not presently <br /> consist of low volume units as specified in the Uniform Plumbing Code(UPC), new low volume <br /> fixtures must be installed. These fixtures (toilets, sinks, etc.)must be checked regularly for leaks <br /> which would cause excessive water flow to the septic tanks. <br /> SEPTIC TANKS <br /> There are presently three - 2,000 gallon septic tanks in series being used for wastewater treatment <br /> from the Temple. Based upon the anticipated sewage flow this, current septic tank capacity <br /> should be adequate. The following calculation indicates there is sufficient detention time: <br /> Detention Time= 6,000 gal tank capacity x 0.70 (30%volume lost to sludge/scum accumu_lation� <br /> 3 (Peaking factor) x 2,500 gallon/day <br /> Detention Time= 0.56 days. The minimum acceptable detention time should be approximately <br /> 0.5 day. This calculation excludes low use of the system Monday through Saturday. <br /> IMPACT MITIGATION <br /> Nitrate-nitrogen impact from the proposed mound system will theoretically be mitigated by the <br /> following design: First, by using three - 2,000 gallon septic tanks in series, there will be a higher <br /> percentage of solid organic material trapped within the tanks. Additionally, a filter should be <br /> installed on the last tank (e.g., Zabel® or OSI®Filters) before the effluent is pumped to the <br /> mound. Secondly, there is evidence that septic tanks have the capability to denitrify nitrate by <br /> the following process: As influent enters the first tank, the wastewater has been aerated from <br /> flushing action, the aerator on faucets, etc. But as the oxygen is consumed by microbiological <br /> processes,the tank becomes anaerobic and the microbes begin to use nitrate as an electron <br /> acceptor. When the effluent reaches the second tank and particularly the third tank,there is <br /> theoretically little oxygen within the tank contents,thus promoting denitrification. This is the <br /> reason 50%nitrogen removal was assigned in the calculations above. Thirdly, as the effluent <br /> travels through the "fill" portion of the mound system, environmental conditions (primarily <br /> aerobic conditions) may promote nitrification. However, when the effluent enters the native clay <br /> soil where the microsites within the clay lattice structure are anaerobic, denitrification should be <br /> promoted. A figure of 25%nitrogen removal by denitrification has been estimated in the above <br /> calculations. <br /> 6 <br /> Valley Ag PSjearch <br />