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Micro-bubble Foam Fractionation System forAquaculture Water Purification

机译:微泡泡沫分馏系统,用于水产养殖净水

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A considerable amount of suspended solids produced in recirculating aquaculture system(RAS) are characterized as fine solids that are toxic to the fish and are extremely difficult to remove bymechanical filtration. A micro-bubble foam fractionation system which consisted of a turbine pump, apressured air-diffusing chamber and a air/water contact column was developed and used forpurification of fish culture water. COD content, turbidity, pH and DO level in the effluent weremeasured over a wide range of operating conditions. Results indicted that increasing the height ofwater column from 0.6 to 1.2m resulted in higher decline in COD content and turbidity in the influent,further increasing the height of the water column to 1.4 m, however, reversed the trend. The highestremoval rate of COD and turbidity (54.47% and 71.47%) occurred at 1.2m of water column.Increasing air flow rate and pressure in the chamber showed significant drop of COD content andturbidity and helped to maintain pH and DO, while water flow rate adversely affect the removalefficiency. Removal rate of COD and turbidity reached to 53.28% and 69.31%, respectively, at theairflow of 0.16m3/h, and reached to 50.5% and 67.66% when the pressure in the chamber was keptat 4.6MPa. Additionally, the removal rate of COD and turbidity dropped to 18.2% and 28.19%,respectively, when water flow rate reached to 950l/h. Slight changes of pH (7.1-7.4) were found inthe effluent, and the changes were well corresponded with that of COD and turbidity. DO level in theeffluent changed from 6.3 to 10.2 mg/l during the experiment.
机译:循环水产养殖系统中产生大量悬浮固体 (RAS)的特征是细小固体,对鱼有毒,极难去除。 机械过滤。微气泡泡沫分馏系统,由涡轮泵, 开发了压力空气扩散室和空气/水接触塔,并将其用于 鱼类养殖用水的净化。废水中的COD含量,浊度,pH和DO水平分别为 在广泛的工作条件下进行测量。结果表明,增加高度 水柱从0.6到1.2m导致进水中COD含量和浊度的下降幅度更大, 进一步将水柱的高度增加到1.4 m,但是,这种趋势得到了扭转。最高的 水柱1.2m处COD去除率和浊度分别为54.47%和71.47%。 腔室内空气流速和压力的增加表明COD含量显着下降,并且 浊度并有助于维持pH和DO,而水流速不利于去除 效率。去除水中COD和浊度分别达到53.28%和69.31%。 空气流量为0.16m3 / h,在保持室内压力的情况下分别达到50.5%和67.66% 在4.6MPa。另外,化学需氧量和浊度的去除率分别下降到18.2%和28.19。 %,分别当水流量达到950l / h时。发现pH值略有变化(7.1-7.4) 废水的变化与COD和浊度的变化非常吻合。 DO水平 在实验过程中,出水从6.3升至10.2 mg / l。

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