The authors carried out a series of experiments in winter and spring of 1974 on the treatment of waste water with a aeration tank (of a nominal capacity for 350 swine) made of FRP equipped with a mechanical aerator of the conventional activated sludge system located in Hikari-machi, Chiba Prefecture, Japan.
The results were as summarized hereunder.
(1) The conditions for the operation of the treatment in winter and spring comprised water temperature in the aeration tank of 14.7±0.2°C and 17.5±1.1°C, respectively, sludge volume at 30 minutes of 94.0±2.4% and 77.8±12.1%, sludge volume indice of 105.0±10.6 and 173.8±16.3, MLSS in the aeration tank of 9, 060±1, 010ppm and 4, 490±595ppm, and MLSS in the returned sludge of 20, 300±2, 330ppm and 7, 260±1, 210ppm, respectively.
(2) The detention time of waste water in the aeration tank were 12.5 hours and 11.5 hours respectively in winter and spring, while BOD loading in kg/m
3 were 1.38±0.34kg/m
3.d and 1.49±0.48kg/m
3.d, in winter and spring, respectively. BOD kg loading per 1kg of MLSS in the aeration tank were 0.15±0.03kg/kg.d (winter) and 0.34±0.10kg/kg.d (spring).
(3) In the test on the functions of the vibration screen, the COD removal ratios determined were 33.5% and 27.9%, respectively in winter and spring at COD consistency of raw waste water of respectively 3, 910±1, 370ppm and 2, 380±1, 080ppm in winter and spring, respectively. SS removal ratios determined then were 23.4% and 28.8% at 7, 740±3, 360ppm and 7, 830±5, 120ppm in winter and spring, respectively.
(4) The capacity for the aeration tank to treat waste water comprised BOD consistency in efferent water of 97.1±16.0ppm in winter and 83.3±12.1ppm in spring and the BOD removal ratios were respectively 93.7% and 94.1%. The SS consistency in efferent was 38.8±13.9ppm in winter and 19.9±4.83ppm in spring, while the SS removal ratios were respectively 97.4% and 99.2%.
The nitrogen removal ratios determined comprised a total nitrogen of 68.8%, ammoniacal nitrogen of 49.2%, and albuminoid nitrogen of 81.8% in winter trial and 64.4%, 41.6%, and 82.5% in spring trial, respectively.
(5) The weights of excess in sludge formed from the aeration tank were 38.82kg/day in the winter trial and 36.17kg/day in the spring trial, which corresponded to 0.53kg/kg and 0.46kg/kg of removed BOD.
(6) BOD removal efficiency per ps. per hour amounted to 1.51kg. BOD/ps H. in the winter trial and 1.64kg BOD/ps. H. in the spring trial, which were about 3 times of that of the method with bubbling aeration of sludge.
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