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METHOD OF COMMONLY TREATING COMMUNAL AND SUGAR MILL WASTE WATERS AND TREATMENT PLANT THEREFOR

机译:共同处理糖厂和糖厂废水及其处理厂的方法

摘要

1. Treatment method for combined municipal and sugar-processing wastewater in a two-stage process, characterized in that tradewaste from sugar processing is digested anaerobically to reduce BOD5 by 80 û 85 percent while municipal sewage is treated in the Stage 1 with the high-rate activated sludge process with organic loadings of 2 - 8 kg BOD5 /kg dry solids per day, achieving through aeration reduction of BOD5 by 60 û 70 percent; after separation of sludge the municipal effluent is mixed with the sugar processing effluent, obtaining mixed effluent of BOD5 in a range of 150 - 300 g/m3, and this combined effluent is further treated in Stage 2 with activated sludge at low loadings of 0.15 - 0.30 kg BOD5 /kg dry solids per day, achieving through aeration reduction of BOD5 to the maximum of 12 g/m3, while excess sludge from both Stages is combined, thickened to 96 percent and digested anaerobically, and at both treatment stages flexible, independent recirculation of sludge is maintained.4. Treatment plant for combined municipal and sugar-processing wastewater, characterized in that consists of trunk municipal sewer (1), screens (2) and grit chamber (3), and aeration tank for Stage 1 (4) that are connected to the intermediate sedimentation tank (5) equipped with the sludge recirculation pipe (6), and intermediate sedimentation tank (5) is connected through the mixing tank (12) with the aeration tank for Stage 2 (14), while the mixing tank (12) is connected to the anaerobic digester (10), while the aeration tank for Stage 2 (14) is connected through the secondary sedimentation tank (15) to the effluent discharge, and the secondary sedimentation tank (15) is equipped with sludge recirculation pipe (16)[...]IMAGE
机译:1.分两步处理市政废水和制糖废水的处理方法,其特征在于,厌氧消化制糖工业产生的贸易废物,使BOD5降低80%至85%,而在第一阶段中,对市政污水进行高浓度的处理。速率为活性污泥法,有机负荷为每天2-8 kg BOD5 / kg干固体,通过将BOD5曝气减少60%至70%来实现;污泥分离后,将城市废水与制糖废水混合,得到BOD5的混合废水在150-300 g / m 3的范围内,并在第二阶段用低负荷的活性污泥进一步处理该合并的废水。每天减少0.15-0.30 kg BOD5 / kg干固体,通过曝气将BOD5减少至最大12 g / m 3,同时将两个阶段的过量污泥合并,增稠至96%并厌氧消化,在两个处理阶段均保持灵活,独立的污泥再循环。4。市政和制糖废水综合处理厂,其特征在于,包括市政干道下水道(1),滤网(2)和沉砂池(3)以及与中间沉淀相连的第一阶段的曝气池(4)配有污泥再循环管(6)的水箱(5)和中间沉淀池(5)通过混合水箱(12)与第二级曝气水箱(14)相连,而混合水箱(12)已连接第二阶段的曝气池(14)通过二级沉淀池(15)连接到废水排放口,而二级沉淀池(15)配有污泥再循环管(16)。 [...] <图像>

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