Methane-driven microbial fuel cells recover energy and mitigate dissolved methane emissions from anaerobic effluents

2018 ◽  
Vol 4 (1) ◽  
pp. 67-79 ◽  
Author(s):  
Siming Chen ◽  
Adam L. Smith

The effluents of mainstream anaerobic treatment processes such as anaerobic membrane bioreactors (AnMBRs) contain dissolved methane that represents a large fraction of the available energy (approximately 50% at 15 °C) and a significant greenhouse gas (GHG) emission if released to the atmosphere.

2011 ◽  
Vol 63 (12) ◽  
pp. 2902-2908 ◽  
Author(s):  
I. Vyrides ◽  
D. C. Stuckey

The treatment of inhibitory (saline) wastewaters is known to produce considerable amounts of soluble microbial products (SMPs), and this has been implicated in membrane fouling; the fate of these SMPs was of considerable interest in this work. This study also investigated the contribution of SMPs to membrane fouling of the; (a) cake layer/biofilm layer, (b) the compounds below the biofilm/cake layer and strongly attached to the surface of the membrane, (c) the compounds in the inner pores of the membrane, and (d) the membrane. It was found that the cake/biofilm layer was the main reason for fouling of the membrane. Interestingly, the bacteria attached to the cake/biofilm layer showed higher biodegradation rates compared with the bacteria in suspension. Moreover, the bacteria attached to the cake layer showed higher amounts of attached extracellular polysaccharides (EPS) compared with the bacteria in suspension, possibly due to accumulation of the released EPS from suspended biomass in the cake/biofilm layer. Molecular weight (MW) analysis of the effluent and reactor bulk showed that the cake layer can retain a large fraction of the SMPs in the reactor and prevent them from being released into the effluent. Hence, while cake layers lead to lower fluxes in submerged anaerobic membrane bioreactors (SAMBRs), and hence higher costs, they can improve the quality of the reactor effluent.


Author(s):  
H. O. Stanley ◽  
C. J. Ugboma

The dynamics of electrochemicals and microbial populations during anaerobic treatment of human urine in soil microbial fuel cells (MFCs) were investigated. The experimental MFC was supplemented with daily urine input while the control MFC was without urine. During the treatment process, electrochemical and microbiological parameters in effluent of the urine-supplemented MFC were monitored using standard methods. The pH of the urine increased from 5.70 to 7.16 after 15 days of treatment in the urine supplemented MFC. The concentration of phosphorus, potassium, sodium, calcium, magnesium, total nitrogen and total organic carbon of the urine reduced from 0.76 g/l to 0.07 g/l, 1.91 g/l to 0.17 g/l, 2.24 g/l to 0.09 g/l, 0.14 g/l to 0.003 g/l, 0.08 g/l to 0.00 g/l, 8.25 g/l to 0.74 g/l and 7.10 g/l to 0.53 g/l respectively after 15 days of treatment. Furthermore, Open voltage of the urine supplemented MFC ranged from 5.63 V to 10.34 V while Open voltage of the control ranged from 1.84 V to 5.02 V after 15 days of operation. The population of facultative bacteria (FAB) and strict anaerobic bacteria (SAB) ranged from 64.2 x 104 CFU to 36.2 x 104 CFU and 21.2 x104 CFU to 61.3 x104 CFU respectively with time. The urine supplemented MFC performed significantly (p < 0.05) better than the control with respect to voltage output while significantly reduced concentrations of organic carbon, nitrogen and metallic (salt) species were found. Therefore, the soil MFC may be applied as a waste management option to treat human urine while generating electricity before disposal.


2011 ◽  
Vol 63 (1) ◽  
pp. 25-31 ◽  
Author(s):  
P. M. Sutton ◽  
H. Melcer ◽  
O. J. Schraa ◽  
A. P. Togna

A new municipal wastewater treatment flowsheet was developed with the objectives of energy sustainability, and water and nutrient recovery. Energy is derived by shunting a large fraction of the organic carbon in the wastewater to an anaerobic digestion system. Aerobic and anaerobic membrane bioreactors play a key role in energy recovery. Phosphorus and nitrogen are removed from the wastewater and recovered through physical-chemical processes. Computer modeling and simulation results together with energy balance calculations, imply the new flowsheet will result in a dramatic reduction in energy usage at lower treatment plant capital costs in comparison to conventional methods.


2016 ◽  
Vol 208 ◽  
pp. 58-63 ◽  
Author(s):  
Kyoung-Yeol Kim ◽  
Wulin Yang ◽  
Yaoli Ye ◽  
Nicole LaBarge ◽  
Bruce E. Logan

2011 ◽  
Vol 63 (9) ◽  
pp. 2004-2009 ◽  
Author(s):  
P. M. Sutton ◽  
B. E. Rittmann ◽  
O. J. Schraa ◽  
J. E. Banaszak ◽  
A. P. Togna

A wastewater-treatment flowsheet was developed to integrate uniquely designed biological processes with physical-chemical unit processes, allowing conversion of the organic carbon in the wastewater to methane, the removal and recovery of phosphorus and nitrogen from the wastewater, and the production of water suitable for reuse. In the flowsheet, energy is derived from the wastewater by first shunting a large fraction of the organic carbon in the wastewater to a solids slurry which is treated via anaerobic digestion. The anaerobic digestion system consists of focused pulsed (FP) pretreatment coupled to anaerobic membrane bioreactors (MBRs). Computer modelling and simulation results are used to optimize design of the system. Energy generation from the system is maximized and costs are reduced by using modest levels of recycle flow from the anaerobic MBRs to the FP pretreatment step.


2010 ◽  
Vol 44 (9) ◽  
pp. 3629-3637 ◽  
Author(s):  
Jeffrey M. Foley ◽  
René A. Rozendal ◽  
Christopher K. Hertle ◽  
Paul A. Lant ◽  
Korneel Rabaey

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