Please use this identifier to cite or link to this item: http://hdl.handle.net/10397/93003
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Title: Toward energy neutrality in municipal wastewater treatment : a systematic analysis of energy flow balance for different scenarios
Authors: Wu, D 
Li, X 
Li, X 
Issue Date: 9-Apr-2021
Source: ACS - ES & T water, 9 Apr. 2021, v. 1, no. 4, p. 796-807
Abstract: To reduce operational costs and carbon footprints, it is highly desirable to achieve energy neutrality in municipal wastewater treatment plants (WWTPs). We reviewed more than 100 nitrification/denitrification (N/DN)- and anaerobic ammonia oxidation (ANAMMOX)-based wastewater treatment systems. The energy consumption performance of N/DN systems ranged from 0.3 to 4 kWh/kg of COD and from 5 to 15 kWh/kg of N, while those of ANAMMOX-based systems ranged from 1 to 5 kWh/kg of COD and from 0.5 to 1.5 kWh/kg of N. According to an energy balance analysis of typical domestic wastewater (COD = 500 mg/L; TN = 50 mg/L) treatment, the conventional N/DN process consumes an average of 0.5 kWh/m3 (1.78 MJ/m3 ) more energy than the amount recovered from the digestion and incineration of its sludge. However, if wastewater is pretreated using a chemically enhanced primary treatment or anaerobic treatment (AT), subsequent ANAMMOX-based wastewater treatment systems may realize WWTP energy autarky or even electricity outputs of ≤0.17 kWh/m3 . In such a nexus of energy recovery, the biogas generation from the AT or the digestion of sludge would be a more effective way to recover energy than the incineration of dewatered digestates. The combination of early stage COD capture and ANAMMOX is a promising approach to achieving sustainable energy performance in future WWTPs.
Keywords: Sewage treatment
ANAMMOX
Biological nitrogen removal
Sludge incineration
Carbon capture
Energy recovery
Publisher: American Chemical Society
Journal: ACS - ES & T water 
EISSN: 2690-0637
DOI: 10.1021/acsestwater.0c00154
Rights: © 2021 American Chemical Society
This document is the Accepted Manuscript version of a Published Work that appeared in final form in ACS ES&T Water, copyright © American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see https://dx.doi.org/10.1021/acsestwater.0c00154
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