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Treatment of ethanolamine using an Fe( III )‐based, two‐chamber microbial fuel cell with continuous Fe( II ) oxidation at the air cathode
Author(s) -
Seo SeokJu,
Shin JaWon,
Maitlo Hubdar Ali,
Park JooYang
Publication year - 2016
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.4731
Subject(s) - microbial fuel cell , ethanolamine , cathode , electrochemistry , ethylenediaminetetraacetic acid , chemistry , ferric , flue gas desulfurization , sulfate , faraday efficiency , chemical engineering , nuclear chemistry , materials science , anode , inorganic chemistry , electrode , chelation , organic chemistry , engineering
BACKGROUND The objective of this study was to investigate the feasibility of developing an integrated bio‐electrochemical system for the removal of ethanolamine from wastewater by combining an Fe( III )‐based microbial fuel cell ( MFC ) with a continuous Fe( II ) oxidation system for simultaneous oxidation and reduction of iron in the same compartment. The ethanolamine in the Fe( III )‐based MFC can be effectively converted to electrical energy by using the catalytic activity of microorganisms. In this respect, the authors investigated whether the introduction of a system for Fe( III ) regeneration could enhance the sustainability of both power generation and the removal of ethanolamine in this integrated system. RESULTS The experimental results obtained with a traditional Fe( III )‐based MFC , operated with a ferric sulfate solution of 25 or 50 mmol L −1 Fe( III ) mixed with ethylenediaminetetraacetic acid ( EDTA ) solution of 10 mmol L −1 , showed that increasing the Fe( III ) concentration leads to improved performance of the MFC ; the maximum power density, open circle voltage ( OCV ), and Coulombic efficiency ( CE ) were all improved. However, the effluents from the cathode chamber contained a low concentration of Fe( III ) due to deficient regeneration of Fe( III ). In the integrated bio‐electrochemical system developed in this work (enhanced Fe( III )‐based MFC ), the generated Fe( II ) was oxidized at the air cathode via favorable oxygen diffusion and a Fe( II )‐based fuel cell ( FC ). CONCLUSION Electricity was sustainably generated from the enhanced MFC with 25 mmol L −1 Fe( III ); the highest performance, in terms of maximum power density, OCV and CE , was achieved using 50 mmol L −1 Fe( III ), thus indicating the increased efficiency of this integrated system. © 2015 Society of Chemical Industry