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Title: An anaerobic-aerobic sequential batch process with simultaneous methanogenesis and short-cut denitrification for the treatment of marine biofoulings

Journal Article · · Waste Management
 [1]
  1. Faculty of Science and Engineering, Soka University, Tangi-machi, Hachioji, Tokyo 192-8577 (Japan)

Highlights: • Combined denitritation–methanogenesis was examined to treat intermittent wastes. • Achieved high NO{sub 2}{sup −} accumulation of 96.4% on average in nitritation. • Achieved high substrate COD removal of 96% in denitritation–methanogenesis. • Intensive effluent exchange enhanced nitrogen removal and decreased CH{sub 4} content. • Daily effluent exchange of 80% could maintain both effluent and biogas qualities. - Abstract: Although combination of denitritation and methanogenesis for wastewater treatment has been widely investigated, an application of this technology to solid waste treatment has been rarely studied. This study investigated an anaerobic-aerobic batch system with simultaneous denitritation-methanogenesis as an effective treatment for marine biofoulings, which is a major source of intermittently discharged organic solid wastes. Preliminary NO{sub 2}{sup −}-exposed sludge was inoculated to achieve stable methanogenesis process without NO{sub 2}{sup −} inhibition. Both high NH{sub 4}{sup +}-N removal of 99.5% and high NO{sub 2}{sup −}-N accumulation of 96.4% were achieved on average during the nitritation step. Sufficient CH{sub 4} recovery of 101 L-CH{sub 4} kg-COD{sup −1} was achieved, indicating that the use of NO{sub 2}{sup −}-exposed sludge is effective to avoid NO{sub 2}{sup −} inhibition on methanogenesis. Methanogenesis was the main COD utilization pathway when the substrate solubilization occurred actively, while denitritation was the main when solubilization was limited because of substrate shortage. The results showed a high COD removal efficiency of 96.0% and a relatively low nitrogen removal efficiency of 64.4%. Fitting equations were developed to optimize the effluent exchange ratio. The estimated results showed that the increase of effluent exchange ratio during the active solubilization period increased the nitrogen removal efficiency but decreased CH{sub 4} content in biogas. An appropriate effluent exchange ratio with high anaerobic effluent quality below approximately 120 mg-N L{sup −1} as well as sufficient CH{sub 4} gas quality which can be used as fuel for gas engine generator was achieved by daily effluent exchange of 80% during the first week and 5% during the subsequent 8 days.

OSTI ID:
22841174
Journal Information:
Waste Management, Vol. 74; Other Information: Copyright (c) 2017 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.; Country of input: International Atomic Energy Agency (IAEA); ISSN 0956-053X
Country of Publication:
United States
Language:
English