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Effect of microbubble generator operating parameters on oxygen transfer efficiency in water

机译:微胶布发生器操作参数对水中氧气转移效率的影响

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This study utilized multistage orifice microbubble generator to investigate dissolved oxygen (DO) formation characteristics and to increase its efficiency, by considering saturator pressure, water supply, and gas flow rates as the main operating factors. The effect of changing the parameters was described in terms of dissolution performance using volumetric mass transfer rate, which is very important element for aerator design and scale-up. Pressure values from 1 to 6atm were taken for the analysis. To improve the oxygen transfer efficiency of the multistage orifice, the internal supply line was controlled to circulate the bubbles water up to 300% cycling. The volumetric mass transfer coefficient was limited below 0.01 per min for air; however, the value varied from 0.10 to 0.13 per min for oxygen at 4.5L/min flow rate, showing increasing pattern with pressure. The transfer characteristic was doubled, with circulating ratio applied, because circulation could multiply the number of microbubbles. Examining the various operating conditions within the range set for the cost to generate 1kg of DO, under gas injection velocity of 1.27m/s, higher liquid pressurization showed lower cost per production in case of oxygen than air. Thus, natural water bottom area environment can be economically improved using oxygen microbubbles, considering the excessive dissolution.
机译:本研究利用多级孔口微泡发生器来研究溶解氧(DO)形成特性并通过考虑饱和压力,供水和气流率作为主要操作因子来提高其效率。通过使用容积传质速率的溶出性能来描述改变参数的效果,这对于曝气器设计和扩展是非常重要的元素。采用1至6ATM的压力值进行分析。为了提高多级孔口的氧气转移效率,控制内部供应管线以将气泡水循环高达300%循环。体积传质系数限制为0.01每分钟的空气;然而,对于4.5L / min流速,该值从0.10到0.13变化为每分钟的氧气流量,表现出增加的压力。转移特性施加循环比率加倍,因为循环可以乘以微泡的数量。检查设定范围内的各种操作条件,以产生1kg DO的成本,在1.27m / s的气体注入速度下,液体加压较高的液体加压在氧气的情况下显示出低于空气。因此,考虑到过量溶解,可以经济地改善天然水底部区域环境。

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