Submersible microbial fuel cell sensor for monitoring microbial activity and BOD in groundwater: Focusing on impact of anodic biofilm on sensor applicability

A sensor, based on a submersible microbial fuel cell (SUMFC), was developed for in situ monitoring of microbial activity and biochemical oxygen demand (BOD) in groundwater. Presence or absence of a biofilm on the anode was a decisive factor for the applicability of the sensor. Fresh anode was required for application of the sensor for microbial activity measurement, while biofilm‐colonized anode was needed for utilizing the sensor for BOD content measurement. The current density of SUMFC sensor equipped with a biofilm‐colonized anode showed linear relationship with BOD content, to up to 250 mg/L (～233 ± 1 mA/m²), with a response time of <0.67 h. This sensor could, however, not measure microbial activity, as indicated by the indifferent current produced at varying active microorganisms concentration, which was expressed as microbial adenosine‐triphosphate (ATP) concentration. On the contrary, the current density (0.6 ± 0.1 to 12.4 ± 0.1 mA/m²) of the SUMFC sensor equipped with a fresh anode showed linear relationship, with active microorganism concentrations from 0 to 6.52 nmol‐ATP/L, while no correlation between the current and BOD was observed. It was found that temperature, pH, conductivity, and inorganic solid content were significantly affecting the sensitivity of the sensor. Lastly, the sensor was tested with real contaminated groundwater, where the microbial activity and BOD content could be detected in <3.1 h. The microbial activity and BOD concentration measured by SUMFC sensor fitted well with the one measured by the standard methods, with deviations ranging from 15% to 22% and 6% to 16%, respectively. The SUMFC sensor provides a new way for in situ and quantitative monitoring contaminants content and biological activity during bioremediation process in variety of anoxic aquifers. Biotechnol. Bioeng. 2011;108: 2339–2347. © 2011 Wiley Periodicals, Inc.     

Anaerobic degradation of solid material: importance of initiation centers for methanogenesis, mixing intensity, and 2D distributed model

Batch anaerobic codigestion of municipal household solid waste (MHSW) and digested manure in mesophilic conditions was carried out. The different waste-to-biomass ratios and intensity of mixing were studied theoretically and experimentally. The experiments showed that when organic loading was high, intensive mixing resulted in acidification and failure of the process, while low mixing intensity was crucial for successful digestion. However, when loading was low, mixing intensity had no significant effect on the process. We hypothesized that mixing was preventing establishment of methanogenic zones in the reactor space. The methanogenic zones are important to withstand inhibition due to development of acids formed during acidogenesis. The 2D distributed models of symmetrical cylinder reactor are presented based on the hypothesis of the necessity of a minimum size of methanogenic zones that can propagate and establish a good methanogenic environment. The model showed that at high organic loading rate spatial separation of the initial methanogenic centers from active acidogenic areas is the key factor for efficient conversion of solids to methane. The initial level of methanogenic biomass in the initiation centers is a critical factor for the survival of these centers. At low mixing, most of the initiation methanogenic centers survive and expand over the reactor volume. However, at vigorous mixing the initial methanogenic centers are reduced in size, averaged over the reactor volume, and finally dissipate. Using fluorescence in situ hybridization, large irregular cocci of microorganisms were observed in the case with minimal mixing, while in the case with high stirring mainly dead cells were found.     

Effects of lipids on thermophilic anaerobic digestion and reduction of lipid inhibition upon addition of bentonite

Summary The effect of bentonite-bound oil on thermophilic anaerobic digestion of cattle manure was investigated. In digestor experiments, addition of oil was found to be inhibitory during start-up and the inhibitory effect was less pronounced when the oil was added in the form of bentonite-bound oil compared to when the oil was added alone. After adaption of the digestors, very rapid degradation of oil was observed and more than 80% of the oil was degraded within a few hours after daily feeding. In batch experiments, glyceride trioleate was found to be inhibitory to thermophilic anaerobic digestion when the concentrations were higher than 2.0 g/l. However, addition of bentonite (a clay mineral) at concentrations of 0.15% and 0.45% was found to partly overcome this inhibition. Addition of calcium chloride in concentration of 3 mM (0.033% w/v) showed a similar positive effect on the utilization of oil, but the effect was lower than with bentonite. Offprint requests to: I. Angelidaki     

Effect of the clay mineral bentonite on ammonia inhibition of anaerobic thermophilic reactors degrading animal waste

Addition of bentonite or the waste product bentonite-bound oil counteracted to some extent the inhibitory effect of ammonia during thermophilic anaerobic digestion of cattle manure. In continuously-fed reactor experiments, addition of bentonite or bentonite-bound oil delayed the onset of the inhibition and aided process recovery after initial inhibition. The effect was observed only when the ammonia concentration was increased gradually, indicating that the major effect of bentonite and BBO was not through a direct antagonistic effect towards ammonia but through an increased process resistance to toxic compounds. In batch experiments bentonite had a similar stimulatory effect leading to a decreased lag phase and increased methane production rate in ammonia inhibited reactors.     

Codigestion of olive oil mill wastewaters with manure, household waste or sewage sludge

Combined anaerobic digestion of oil mill effluent(OME) together with manure, household waste (HHW) orsewage sludge was investigated. In batch experimentsit was shown that OME could be degraded into biogaswhen codigested with manure. In codigestion with HHWor sewage sludge, OME dilution with water (1:5) wasrequired in order to degrade it. Using continuouslystirred lab-scale reactors it was shown thatcodigestion of OME with manure (50:50 and 75:25 OMEto manure ratios) was successful with a theoreticalOME utilization of 75% and with approx. 87%reduction of the lipids content in OME. An OMEutilization of approx. 55%, and lipid reduction of73% was reached in codigestion with HHW (50:50 and75:25 OME to HHW ratios). The results showed thatthe high buffering capacity contained in manure,together with the content of several essentialnutrients, make it possible to degrade OME withoutprevious dilution, without addition of externalalkalinity and without addition of external nitrogensource.     

Self-stacked submersible microbial fuel cell (SSMFC) for improved remote power generation from lake sediments

Electric energy can be harvested from aquatic sediments by utilizing microbial fuel cells (MFCs). A main challenge of this application is the limited voltage output. In this study, an innovative self-stacked submersible MFC (SSMFC) was developed to improve the voltage generation from lake sediments. The SSMFC successfully produced a maximum power density of 294 mW/m(2) and had an open circuit voltage (OCV) of 1.12 V. However, voltage reversal was observed in one cell at high current density. Investigation on the cause for voltage reversal revealed that voltage reversal was occurring only when low external resistance (≤ 400Ω in this study) was applied. In addition, the internal resistance and OCV were the most important parameters for predicting which cell unit had the highest probability to undergo voltage reversal. Use of a capacitor was found to be an effective way to prevent voltage reversal and at the same time store power. These results provide new insight into the development of effective MFC system, capable of extracting energy and promoting bioremediation of organic pollutants from sediments.     

Biohydrogen production in granular up-flow anaerobic sludge blanket (UASB) reactors with mixed cultures under hyper-thermophilic temperature (70 degrees C)

Hyper-thermophilic hydrogen production without methane was demonstrated for the first time in granular up-flow anaerobic sludge blanket (UASB) system fed with glucose using mixed cultures. The maximum hydrogen yield in this study was 2.47 +/- 0.15 mol H2/mol glucose. This high yield has never been previously reported in mixed culture systems and it was likely due to more favorable thermodynamic conditions at hyper-thermophilic temperatures. Different start-up strategies (bromoethanosulfonate (BES) addition and flow recycle) were evaluated. BES addition during start-up prevented the establishment of methanogenic cultures in granules. Flow recycle was important to achieve higher hydrogen yield through enriching better hydrogen-producing organisms and reduced the start-up period as well. This study indicated UASB system was a promising system for hydrogen production.     

Anammox for ammonia removal from pig manure effluents: Effect of organic matter content on process performance

The anammox process, under different organic loading rates (COD), was evaluated using a semi-continuous UASB reactor at 37 °C. Three different substrates were used: initially, synthetic wastewater, and later, two different pig manure effluents (after UASB-post-digestion and after partial oxidation) diluted with synthetic wastewater. High ammonium removal was achieved, up to 92.1 ± 4.9% for diluted UASB-post-digested effluent (95 mg COD L^?1) and up to 98.5 ± 0.8% for diluted partially oxidized effluent (121 mg COD L^?1). Mass balance clearly showed that an increase in organic loading (from 95 mg COD L^?1 to 237 mg COD L^?1 and from 121 mg COD L^?1 to 290 mg COD L^?1 for the UASB-post-digested effluent and the partially oxidized effluent, respectively) negatively affected the anammox process and facilitated heterotrophic denitrification. Partial oxidation as a pre-treatment method improved ammonium removal at high organic matter concentration. Up to threshold organic load concentration of 142 mg COD L^?1 of UASB-post-digested effluent and 242 mg COD L^?1 of partially oxidized effluent, no effect of organic loading on ammonia removal was registered (ammonium removal was above 80%). However, COD concentrations above 237 mg L^?1 (loading rate of 112 mg COD L^?1 day^?1) for post-digested effluent and above 290 mg L^?1 (loading rate of 136 mg COD L^?1 day^?1) for partially oxidized effluent resulted in complete cease of ammonium removal. Results obtained showed that, denitrification and anammox process were simultaneously occurring in the reactor. Denitrification became the dominant ammonium removal process when the COD loading was increased.     

Generation of Electricity and Analysis of Microbial Communities in Wheat Straw Biomass-Powered Microbial Fuel Cells

Electricity generation from wheat straw hydrolysate and the microbial ecology of electricity-producing microbial communities developed in two-chamber microbial fuel cells (MFCs) were investigated. The power density reached 123 mW/m² with an initial hydrolysate concentration of 1,000 mg chemical oxygen demand (COD)/liter, while coulombic efficiencies ranged from 37.1 to 15.5%, corresponding to the initial hydrolysate concentrations of 250 to 2,000 mg COD/liter. The suspended bacteria found were different from the bacteria immobilized in the biofilm, and they played different roles in electricity generation from the hydrolysate. The bacteria in the biofilm were consortia with sequences similar to those of Bacteroidetes (40% of sequences), Alphaproteobacteria (20%), Bacillus (20%), Deltaproteobacteria (10%), and Gammaproteobacteria (10%), while the suspended consortia were predominately Bacillus (22.2%). The results of this study can contribute to improving understanding of and optimizing electricity generation in microbial fuel cells.Wheat straw is one of the most abundant renewable resources. According to the Food and Agriculture Organization of the United Nations, approximately 1.9 × 10⁹ tons of wheat straw annually are produced worldwide, accompanied by 6.2 × 10⁸ tons of wheat production. Wheat straw is composed of 35 to 45% cellulose and 20 to 30% hemicelluloses with a relatively low lignin content (<20%) (42). The hemicellulose fraction of the straw is easily hydrolyzed to its constituent sugars by a hydrothermal treatment process, forming a carbohydrate-enriched liquid hydrolysate (46). Chemical and biological approaches to sustainable energy production from the liquefied hydrolysates to energy carriers, such as methane, ethanol, and H₂, have been developed. However, many of these approaches encounter technical and economical hurdles (10, 12, 15, 16). An alternative strategy is direct conversion of wheat straw biomass to electrical energy in microbial fuel cells (MFCs).MFCs are bioelectrochemical reactors in which microorganisms mediate the direct conversion of chemical energy stored in organic matter or bulk biomass into electrical energy (12, 15, 16, 40). Various substrates, such as simple carbohydrates, low-molecular-weight organic acids, starch, amino acids, chitin, cellulose, domestic wastewater, food-processing wastewater, recycled paper wastewater, and marine sediment organic matter, have been successfully utilized for power generation in MFCs (16-18, 27, 30, 33). To understand the microbial constraints on various fuel-powered MFCs, microbial communities have been characterized by several groups. Microbial communities from various systems are very different and often diverse, ranging from well-known metal- and anode-reducing bacteria to unknown exoelectrogens (1, 20, 21). It has been found that parameters such as the substrates used as fuels and the inocula used for starting up the MFCs can influence the anode bacterial communities in an MFC, which subsequently influence the efficiency of the MFCs (3, 14, 22, 38, 44). Different pure substrates, such as acetate, glucose, and lactate, were used as fuel to compare the microbial communities that developed in the MFCs. Regardless of the different substrates, all anode communities contained sequences closely affiliated with Geobacter sulfurreducens (>99% similarity) and an uncultured bacterium clone belonging to the family Bacteroidaceae (99% similarity). Firmicutes were only found in glucose-fed MFCs (20). Microbial-community analyses of MFCs powered with complex substrates have also been performed by several researchers, and their results were very diverse. The microbial community in starch wastewater-powered MFC was dominated by unidentified bacteria (35.9%), followed by Betaproteobacteria (25.0%), Alphaproteobacteria (20.1%), and the Cytophaga/Flexibacter/Bacteroides group (19.0%) (21). The anode-attached consortia in a cellulose-powered MFC were related to Clostridium spp., while Comamonas spp. were abundant in the suspended consortia (13). Although many studies have reported the microbial compositions of MFCs, it is still unclear which microbial communities develop as a function of the external parameters.Wheat straw biomass constitutes a large source for bioenergy production and shows promising prospects for electricity generation in MFCs. Therefore, wheat straw biomass was used to study the microbial communities that develop during the operation of an MFC in order to better understand the microbial electrochemical roles and potentially improve MFC performance.The objectives of this study were to (i) test wheat straw hydrolysate as a potential fuel in an MFC for electricity generation and (ii) study the microbial composition and evolution of electricity-producing communities in a two-chamber MFC system. Phylogenetic-diversity analysis of the enriched consortia was conducted to verify the presence of hydrolytic and respiratory anaerobes that could couple hydrolysate oxidation with proton reduction in the anode chamber. This is the first report of exploiting microbial communities for direct conversion of wheat straw hydrolysate to electrical energy in an MFC.