Yao Kangning, Chi Yong, Wang Fei, Yan Jianhua, Ni Mingjiang, Cen Kefa
State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027, China E-mail:
Water Sci Technol. 2016;73(8):1969-77. doi: 10.2166/wst.2016.018.
A commonly used aeration device at present has the disadvantages of low mass transfer rate because the generated bubbles are several millimeters in diameter which are much bigger than microbubbles. Therefore, the effect of a microbubble on gas-liquid mass transfer and wastewater treatment process was investigated. To evaluate the effect of each bubble type, the volumetric mass transfer coefficients for microbubbles and conventional bubbles were determined. The volumetric mass transfer coefficient was 0.02905 s(-1) and 0.02191 s(-1) at a gas flow rate of 0.67 L min(-1) in tap water for microbubbles and conventional bubbles, respectively. The degradation rate of simulated municipal wastewater was also investigated, using aerobic activated sludge and ozone. Compared with the conventional bubble generator, the chemical oxygen demand (COD) removal rate was 2.04, 5.9, 3.26 times higher than those of the conventional bubble contactor at the same initial COD concentration of COD 200 mg L(-1), 400 mg L(-1), and 600 mg L(-1), while aerobic activated sludge was used. For the ozonation process, the rate of COD removal using microbubble generator was 2.38, 2.51, 2.89 times of those of the conventional bubble generator. Based on the results, the effect of initial COD concentration on the specific COD degradation rate were discussed in different systems. Thus, the results revealed that microbubbles could enhance mass transfer in wastewater treatment and be an effective method to improve the degradation of wastewater.
目前常用的曝气装置存在传质速率低的缺点,因为产生的气泡直径为几毫米,比微气泡大得多。因此,研究了微气泡对气液传质及废水处理过程的影响。为了评估每种气泡类型的效果,测定了微气泡和常规气泡的体积传质系数。在自来水中,当气体流量为0.67 L min(-1)时,微气泡和常规气泡的体积传质系数分别为0.02905 s(-1)和0.02191 s(-1)。还使用好氧活性污泥和臭氧研究了模拟城市废水的降解率。与常规气泡发生器相比,在相同的初始化学需氧量(COD)浓度分别为200 mg L(-1)、400 mg L(-1)和600 mg L(-1)且使用好氧活性污泥的情况下,微气泡发生器的化学需氧量(COD)去除率比常规气泡接触器分别高2.04倍、5.9倍和3.26倍。对于臭氧化过程,使用微气泡发生器的化学需氧量(COD)去除率是常规气泡发生器的2.38倍、2.51倍和2.89倍。基于这些结果,讨论了不同系统中初始化学需氧量(COD)浓度对特定化学需氧量(COD)降解率的影响。因此,结果表明微气泡可以增强废水处理中的传质,是提高废水降解的有效方法。