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Concentrating Organic Matters in Sewage using Forward Osmosis Membrane Treatment for Energy Production by Methane Fermentation

机译:使用正渗透膜处理浓缩废水中的有机物,以通过甲烷发酵生产能量

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The activated sludge process is widely used for sewage treatment, and the power consumption for aeration and the disposal of excess sludge are inevitable problems. The methane fermentation process is anaerobic process that requires no aeration, can produce energy and generate less excess sludge. However, sewage treatment using methane fermentation is difficult due to too low concentration of organic matters in sewage. Application of forward osmosis (FO) membrane treatment has been examined as the concentrating method of sewage. In this study, the effects of the operating pressure to the water permeate flux, reverse salt passage ratio of NaCl, and concentration ratio of organic matter were evaluated in concentrating of sewage using seawater. The water permeate flux was increased from 0.05 to 0.75 m/d as the operating pressure increased from 0 to 1.0 MPa, the operating pressure was effective factor for improvement of the flux. Moreover, increase of the pressure made the concentration ratio of organic matter increased and made the reverse salt passage ratio from seawater to sewage decreased. It became clear that the inhibition of methane fermentation by NaCl is suppressed by pressurization in concentrating of sewage using FO membrane treatment.
机译:活性污泥法被广泛用于污水处理,曝气的功率消耗和剩余污泥的处理是不可避免的问题。甲烷发酵过程是厌氧过程,不需要曝气,可以产生能量并产生较少的剩余污泥。但是,由于污水中有机物的浓度太低,使用甲烷发酵的污水处理是困难的。作为污水的浓缩方法,正渗透膜(FO)膜处理的应用已得到检验。在这项研究中,在使用海水浓缩废水时,评估了工作压力对渗透通量,NaCl的反盐通过率和有机物浓度比的影响。随着工作压力从0 MPa增加到1.0 MPa,渗透水通量从0.05 m / d增加到0.75 m / d,工作压力是改善通量的有效因素。此外,压力的增加使有机物的浓度比增加,并且使从海水到污水的反盐通过率降低。显而易见的是,通过使用FO膜处理浓缩污水中的压力,可以抑制NaCl对甲烷发酵的抑制作用。

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