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Process optimisation of a combined system of floating medium and sand filter in prawn farm effluent treatment

机译:对虾养殖场污水处理中浮沙滤池联合系统的工艺优化

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A treatment technology known as " a combined system of Boating medium and sand filter (FMSF)" was developed and tested successfully with prawn farm effluent. This system has a remarkable technoeconomical advantages. Laboratory and semi pilot-scale studies were carried out to optimise the Biter bed depth, backwash method and other operating conditions. The dewatering characteristics of sludge from filter backwash was also analysed. The filter was operated at a high rate. The experimental results indicated that:; (i) in case of no in-line chemical addition, the smaller ratio between floating medium and sand filter depth gave rise better filter performance. At the filtration rate of 7.5 - 20 m(3)/m(2).h and with an in-line chemical addition, the suitable depth of floating medium varied from 400-1000 mm for a sand filter depth of 400 mm; (ii) frequent (once in every 90-120 minutes) but short duration of backwash (not more than 60 seconds) was found to be suitable. During the backwash, the water and air were sent for 30 seconds in upward direction and then followed with upflow of water for another 30 seconds. Backwash water amount comprised only 1.2-1.8% of the filtered water production. A mechanical backwash system using rotating paddles is a promising alternative for floating medium filter; and (iii) the filterability of the sludge from filter backwash was low in case of no in-line chemical addition (specific resistance, r = 9.34 x 10(10) m/kg) but improved with in-line flocculant addition (r = 3.07 x 10(9) - 1.29 x 10(10) m/kg). (C) 1998 Elsevier Science Ltd. All rights reserved. [References: 9]
机译:开发了一种称为“划船中型滤池和砂滤池的组合系统(FMSF)”的处理技术,并成功地对虾养殖场废水进行了测试。该系统具有显着的技术经济优势。进行了实验室和中试规模的研究,以优化Biter床深度,反洗方法和其他操作条件。还分析了过滤器反冲洗产生的污泥的脱水特性。过滤器的运行速度很高。实验结果表明: (i)在不添加在线化学药剂的情况下,漂浮介质与砂滤深度之间的比例越小,过滤性能越好。在过滤速度为7.5-20 m(3)/ m(2).h的情况下,加上在线化学添加,对于深度为400 mm的砂滤池,漂浮介质的合适深度为400-1000 mm; (ii)经常(每90-120分钟一次),但反洗时间短(不超过60秒)是合适的。在回洗过程中,水和空气沿向上方向输送30秒,然后再向上流动30秒。反冲洗水量仅占过滤水产量的1.2-1.8%。使用旋转桨的机械反冲洗系统是浮动介质过滤器的有前途的替代方法。 (iii)在不添加在线化学药剂的情况下,过滤器反冲洗产生的污泥的过滤性较低(电阻率,r = 9.34 x 10(10)m / kg),但是通过添加在线絮凝剂,污泥的过滤性得到改善(r = 3.07 x 10(9)-1.29 x 10(10)m / kg)。 (C)1998 Elsevier ScienceLtd。保留所有权利。 [参考:9]

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