A whole system for the automatic removal of waste and treated effluent and installment to flush out the waste from a 500-pig unit was constructed in YORII, and was started operating on June 3, 1970. The installment for conventional activated sludge was erected by the financial aid of Ministry of Agriculture and Forestry and Saitama Prefecture. National Institute of Animal Industry sponsored it as a demonstration project. Figure 1 is a flow chart of the total plant. During the 2 years of operation for the study of BOD, SS, T-N the main emphasis was on assessing and demonstrating the technical and ecological feasibility of the holding of waste and treated effluent without creating gross water pollution nor odor nuisance.
The results were as follows:
1) The flushing water carries the dung from the animal barns deferated on the gutter to a sump, from where the waste water is pumped onto a stainless steel screen. Through the screen, the solids are separated from the liquids. Clean water is added to the liquids and mixed, diluted, and discharged into the conventinal activated sludge, and clarified. Meanwhile, the solids separated by the screen, are transported by the dump car onto the mulberry field. In the aeration tank activated sludge, return sludge diluted liquids were mixed. After 12 hours treatment, the supernatant from the settling tanks is overflown into the sludge concentrating tanks, and the final supernatant is filtered through the chlorine disinfection equipment and overflown into the river.
2) During the 2 years of operation, average influent BOD onto the screen was 3, 530±1, 400ppm. At the screen, the BOD was separated from liquids. Liquid BCD was 2, 750±1, 048ppm. Average Suspended Solids (SS) in the screen was 5, 160±2, 475ppm. At the screen, the SS was separated from liquids. Average SS was 3, 850±1, 680ppm.
3) During optimum operation of the plant (BOD load 0.50kg/M/day), the pH of the mixed liquor remained in a favorable range between 6.5 to 7.0. Mixed Liquor Suspended Solids (MLSS) remained at an optimum level of around 7, 800ppm and ranged from 5, 000 to 12, 900ppm during the first one year. Average influent SS in aeration tank during the first one year of operation was 1, 580ppm, and ranged from 430 to 2, 800ppm. But the effluent water SS remained in the range of 14 to 151ppm and average 70ppm. Average influent BOD in aeration tank was 1, 100ppm and ranged from 450 to 130ppm and average 70ppm.
4) We felt that we needed to devise a very simple test which could be run the farm to monitor the efficiency of the plant. Sludge Volume (SV) was such a test. SV is an excellent index of the level of effiency of the plant. During the first one year of operation, the SV of the mixed liquor averaged 30%.
5) Temperature of the mixed liquor was in the range of 7°C to 23.1°C during the period of operation, but decresed to 7°C-11°C after the winter operation.
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