TY - JOUR
T1 - Total nitrogen removal in a single-chamber, plug-flow microbial fuel cell
AU - Butler, Caitlyn S.
AU - Pavissich, Juan Pablo
AU - Nerenberg, Robert
PY - 2010
Y1 - 2010
N2 - Microbial fuel cells (MFCs) can produce energy while removing BOD from wastewater, and MFCs with a biocathode can additionally achieve denitrification. However, MFCs cannot achieve nitrification. We propose a novel plug-flow MFC for BOD and total nitrogen removal, where nitrifying hollow-fiber membranes (HFMs) are integrated into the cathode. The process consists of a plug-flow reactor receiving BOD and ammonium. BOD is oxidized at the anode. Protons from BOD oxidzation and the influent ammonium, are conveyed by the flow to the cathode. In the cathode, racks of nitrifying HFMs are alternated with denitrifying biocathodes, providing nitrification and denitrification. No proton exchange membrane (PEM) is required and pH shifts are minimized. This configuration obtained a power density of 296 mW/m3 (5 mW/m2 cathode) and a coulombic efficiency of 17%. Nitrification and denitrification fluxes were up to 1.7 g NH4+-N/m2 HFM/d and 1.6 g NO3--N/m2 cathode/d, respectively. We currently are developing a mathematical model to identify optimal operating conditions and potential configurations for scale-up.
AB - Microbial fuel cells (MFCs) can produce energy while removing BOD from wastewater, and MFCs with a biocathode can additionally achieve denitrification. However, MFCs cannot achieve nitrification. We propose a novel plug-flow MFC for BOD and total nitrogen removal, where nitrifying hollow-fiber membranes (HFMs) are integrated into the cathode. The process consists of a plug-flow reactor receiving BOD and ammonium. BOD is oxidized at the anode. Protons from BOD oxidzation and the influent ammonium, are conveyed by the flow to the cathode. In the cathode, racks of nitrifying HFMs are alternated with denitrifying biocathodes, providing nitrification and denitrification. No proton exchange membrane (PEM) is required and pH shifts are minimized. This configuration obtained a power density of 296 mW/m3 (5 mW/m2 cathode) and a coulombic efficiency of 17%. Nitrification and denitrification fluxes were up to 1.7 g NH4+-N/m2 HFM/d and 1.6 g NO3--N/m2 cathode/d, respectively. We currently are developing a mathematical model to identify optimal operating conditions and potential configurations for scale-up.
UR - http://www.scopus.com/inward/record.url?scp=79951534625&partnerID=8YFLogxK
M3 - Conference article
AN - SCOPUS:79951534625
SN - 0065-7727
JO - ACS National Meeting Book of Abstracts
JF - ACS National Meeting Book of Abstracts
T2 - 239th ACS National Meeting and Exposition
Y2 - 21 March 2010 through 25 March 2010
ER -