Factors affecting microbial fuel cell acclimation and operation in temperate climates

2013 ◽  
Vol 67 (11) ◽  
pp. 2568-2575 ◽  
Author(s):  
I. S. Michie ◽  
J. R. Kim ◽  
R. M. Dinsdale ◽  
A. J. Guwy ◽  
G. C. Premier

For the successful scale-up of microbial fuel cell (MFC) systems, enrichment strategies are required that not only maximise reactor performance but also allow anodic biofilms to be robust to environmental change. Cluster analysis of Denaturing Gradient Gel Electrophoresis community fingerprints showed that anodic biofilms were enriched according to substrate type and temperature. Acetate produced the highest power density of 7.2 W m−3 and butyrate the lowest at 0.29 W m−3, but it was also found that the trophic conditions used to acclimate the electrogenic biofilms also determined the MFC response to different substrate types, with both acetate and butyrate substrates recording power densities of 1.07 and 1.0 W m−3 respectively in a sucrose enriched reactor. When temperature perturbations were introduced to investigate the stability of the different substrate acclimated electrogenic biofilms, the 20 °C acclimated acetate reactor was unaffected by 10 °C operation but all reactors acclimated at 35 °C were adversely affected. When the operating temperature was raised back to 35 °C both the acetate and butyrate reactors recovered electrogenic activity but the sucrose reactor did not. It is thought that this was due to the more complex syntropic interactions that are required to occur when metabolising more complex substrate types.

RSC Advances ◽  
2016 ◽  
Vol 6 (113) ◽  
pp. 111657-111665 ◽  
Author(s):  
Hend Omar Mohamed ◽  
M. Obaid ◽  
Ahmed S. Yasin ◽  
Jun Hee Kim ◽  
Nasser A. M. Barakat

The properties and cost of anode materials are essential factors affecting the microbial fuel cell (MFC) performance.


2013 ◽  
Vol 68 (9) ◽  
pp. 1914-1919 ◽  
Author(s):  
Gai-Xiu Yang ◽  
Yong-Ming Sun ◽  
Xiao-Ying Kong ◽  
Feng Zhen ◽  
Ying Li ◽  
...  

Microbial fuel cells (MFCs) are devices that exploit microorganisms as biocatalysts to degrade organic matter or sludge present in wastewater (WW), and thereby generate electricity. We developed a simple, low-cost single-chamber microbial fuel cell (SCMFC)-type biochemical oxygen demand (BOD) sensor using carbon felt (anode) and activated sludge, and demonstrated its feasibility in the construction of a real-time BOD measurement system. Further, the effects of anodic pH and organic concentration on SCMFC performance were examined, and the correlation between BOD concentration and its response time was analyzed. Our results demonstrated that the SCMFC exhibited a stable voltage after 132 min following the addition of synthetic WW (BOD concentration: 200 mg/L). Notably, the response signal increased with an increase in BOD concentration (range: 5–200 mg/L) and was found to be directly proportional to the substrate concentration. However, at higher BOD concentrations (>120 mg/L) the response signal remained unaltered. Furthermore, we optimized the SCMFC using synthetic WW, and tested it with real WW. Upon feeding real WW, the BOD values exhibited a standard deviation from 2.08 to 8.3% when compared to the standard BOD5 method, thus demonstrating the practical applicability of the developed system to real treatment effluents.


2022 ◽  
Vol 520 ◽  
pp. 230875
Author(s):  
Xavier Alexis Walter ◽  
Elena Madrid ◽  
Iwona Gajda ◽  
John Greenman ◽  
Ioannis Ieropoulos

2003 ◽  
Vol 47 (9) ◽  
pp. 123-128 ◽  
Author(s):  
A. Pruden ◽  
M. Sedran ◽  
M. Suidan ◽  
A. Venosa

An aerobic fluidized bed reactor (FBR) was operated for the removal of methyl tert-butyl ether (MTBE) and benzene, toluene, ethylbenzene, and p-xylene (BTEX) from water. The reactor was seeded with a mixed culture adapted to MTBE. Granular activated carbon (GAC) was used as the biological attachment medium. Influent MTBE to the reactor was 7.8 mg/L MTBE, with a flow rate of 22.7 L/day, and an empty bed contact time of 1 hour. The acclimation period required was relatively short, about 30 days before reaching an average stable effluent concentration of 18.5 ± 10 μg/L. BTEX was introduced to the feed at an equivalent chemical oxygen demand (COD) as the MTBE at day 225 and was biodegraded spontaneously with no apparent acclimation period required. The average influent of each of the four BTEX compounds was about 2 mg/L, and the range of the average effluent concentrations was 1.4-2.2 μg/L. After achieving 180 days of stable performance with BTEX addition, the total flow rate to the reactor was gradually increased by 20% increments to 160% of the original flow (36.4 L/day). Increases by 20% and 40% had no apparent effect on reactor performance, but increase by 60% required 30 days before effluent quality returned to previous values. Composition of the culture was monitored throughout operation of the reactor using denaturing gradient gel electrophoresis (DGGE). The culture consisted of Flavobacteria-Cytophaga and organisms with high similarity to the known MTBE degrader PM1.


2015 ◽  
Vol 7 (4) ◽  
pp. 043101 ◽  
Author(s):  
N. Samsudeen ◽  
Amit Sharma ◽  
T. K. Radhakrishnan ◽  
Manickam Matheswaran

2000 ◽  
Vol 66 (9) ◽  
pp. 3814-3822 ◽  
Author(s):  
Charles R. Lovell ◽  
Yvette M. Piceno ◽  
Joseph M. Quattro ◽  
Christopher E. Bagwell

ABSTRACT N2 fixation by diazotrophic bacteria associated with the roots of the smooth cordgrass, Spartina alterniflora, is an important source of new nitrogen in many salt marsh ecosystems. However, the diversity and phylogenetic affiliations of these rhizosphere diazotrophs are unknown. Denaturing gradient gel electrophoresis (DGGE) of PCR-amplified nifH sequence segments was used in previous studies to examine the stability and dynamics of the Spartina rhizosphere diazotroph assemblages in the North Inlet salt marsh, near Georgetown, S.C. In this study, plugs were taken from gel bands from representative DGGE gels, thenifH amplimers were recovered and cloned, and their sequences were determined. A total of 59 sequences were recovered, and the amino acid sequences predicted from them were aligned with sequences from known and unknown diazotrophs in order to determine the types of organisms present in the Spartina rhizosphere. We recovered numerous sequences from diazotrophs in the γ subdivision of the division Proteobacteria(γ-Proteobacteria) and from various anaerobic diazotrophs. Diazotrophs in the α-Proteobacteria were poorly represented. None of the Spartina rhizosphere DGGE band sequences were identical to any known or previously recovered environmental nifH sequences. TheSpartina rhizosphere diazotroph assemblage is very diverse and apparently consists mainly of unknown organisms.


Processes ◽  
2021 ◽  
Vol 9 (6) ◽  
pp. 985
Author(s):  
Wei Han Tan ◽  
Siewhui Chong ◽  
Hsu-Wei Fang ◽  
Kuan-Lun Pan ◽  
Mardawani Mohamad ◽  
...  

Microbial fuel cell (MFC) technology has attracted a great amount of attention due to its potential for organic and inorganic waste treatment concomitant with power generation. It is thus seen as a clean energy alternative. Modifications and innovations have been conducted on standalone and hybrid/coupled MFC systems to improve the power output to meet the end goal, namely, commercialization and implementation into existing wastewater treatment plants. As the energy generated is inversely proportional to the size of the reactor, the stacking method has been proven to boost the power output from MFC. In recent years, stacked or scale-up MFCs have also been used as a power source to provide off-grid energy, as well as for in situ assessments. These scale-up studies, however, encountered various challenges, such as cell voltage reversal. This review paper explores recent scale-up studies, identifies trends and challenges, and provides a framework for current and future research.


2021 ◽  
Vol 24 (1) ◽  
pp. 14-20
Author(s):  
Xiuwei Fu ◽  
Li Fu ◽  
Hashem Imani Marrani

The microbial fuel cell is one of the most important tools in the supply of renewable energy and its controller plays an important role in improving the performance and stability of its output. Using the advantages of adaptive and sliding mode methods, this paper presents a combined technique to ensure the stability and output voltage stabilization of the fuel cell in the presence of parametric uncertainties and nonlinear terms. The proposed control method is compared with classical control approaches and the simulation results confirm its efficiency.


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