Continuous electricity production from artificial wastewater using a mediator-less microbial fuel cell

A microbial fuel cell (MFC) was optimized in terms of MFC design factors and operational parameters for continuous electricity production using artificial wastewater (AW). The performance of MFC was analyzed through the polarization curve method under different conditions using a mediator-less MFC. The highest power density of 0.56 W/m2 was achieved with AW of 300 mg/l fed at the rate of 0.53 ml/min at 35 degrees C. The power per unit cell working volume was 102 mW/l, which was over 60 times higher than those reported in the previous mediator-less MFCs which did not use a cathode or an anode mediator. The power could be stably generated over 2 years.     

Continuous measurement of microbial heat production in laboratory fermentors

The possibility of continuously measuring the heat produced by microorganisms in an ordinary laboratory fermentor was studies. An inventory of the heat flows influencing the temperature of the culture was made. The magnitude and standard deviation in these heat flows were studied from theoretical and practical viewpoints. Calibration procedures were tested, and a model describing the heat flows in steady state and during dynamic conditions was made. Microbial heat production could be calculated accurately with the help of this model, appropriate temperature measurements, and equipment properties measured during the calibration procedures. It was found that the measurement of heat production could be done with an accuracy similar to that in the O(2) uptake measurement. (c) 1993 John Wiley & Sons, Inc.     

Continuous fermentation of wheat-supplemented lignocellulose hydrolysate with different types of cell retention

Medium supplementation and process alternatives for fuel ethanol production from dilute acid lignocellulose hydrolysate were investigated. Dilute acid lignocellulose hydrolysate supplemented with enzymatically hydrolysed wheat flour could sustain continuous anaerobic cultivation of Saccharomyces cerevisiae ATCC 96581 if further supplemented with ammonium sulphate and biotin. This medium composition allowed for a hexose utilisation of 73% and an ethanol production of 36 mmol l(-1) h(-1) in chemostat cultivation at dilution rate 0.10 h(-1). Three different methods for cell retention were compared for improved fermentation of supplemented lignocellulose hydrolysate: cell recirculation by filtration, cell recirculation by sedimentation and cell immobilisation in calcium alginate. All three cell retention methods improved the hexose conversion and increased the volumetric ethanol production rate. Recirculation of 75% of the bioreactor outlet flow by filtration improved the hexose utilisation from 76% to 94%. Sedimentation turned out to be an efficient method for cell separation; the cell concentration in the reactor was 32 times higher than in the outflow after 60 h of substrate feeding. However, chemostat and continuous cell recirculation cultures became severely inhibited when the dilution rate was increased to 0.20 h(-1). In contrast, an immobilised system kept producing ethanol at a stable level also at dilution rate 0.30 h(-1).     

Continuous ethanol production using cell recycle with a settler

Summary A system for a high-density culture of Zymomonas mobilis was tested using a reactor with cell recycle by means of a simple settler. Growth-limiting conditions were created by raising the temperature and lowering the amount of yeast-extract. In this case the biomass production decreased, while the specific ethanol productivity did not change markedly. Under these conditions we succeeded in creating a system with a productivity of 40.5 g.1^-1.h^-1. The choice for optimal design of the settler and optimal conditions has to be made by optimization taking into account economic and whole process considerations.     

Continuous culture of bacteria with biomass retention

Bacterial cells have three phases of growth which are characterized respectively by: (1) balanced growth with a high yield of biomass; (2) balanced growth with lower biomass yield; and (3) unbalanced growth with lowest biomass yield. Phases 2 and 3 are associated with elevated concentrations of the regulatory nucleotides centered on guanosine-5′-diphosphate-3′-diphosphate. Maintenance of the correct growth phase is important in optimizing industrial product formation by bacterial populations.     

Continuous flow membrane-less air cathode microbial fuel cell with spunbonded olefin diffusion layer

The power production performance of a membrane-less air-cathode microbial fuel cell was evaluated for 53 days. Anode and cathode electrodes and the micro-fiber cloth separator were configured by sandwiching the separator between two electrodes. In addition, the air-facing side of the cathode was covered with a spunbonded olefin sheet instead of polytetrafluoroethylene (PTFE) coating to control oxygen diffusion and water loss. The configuration resulted in a low resistance of about 4Ω and a maximum power density of 750 mW/m2. However, as a result of a gradual decrease in the cathode potential, maximum power density decreased to 280 mW/m2. The declining power output was attributed to loss of platinum catalyst (8.26%) and biomass growth (38.44%) on the cathode. Coulombic efficiencies over 55% and no water leakage showed that the spunbonded olefin sheet covering the air-facing side of the cathode can be a cost-effective alternative to PTFE coating.     

Continuous production of glutathione using immobilized microbial cells containing ATP generating system

Acetate kinase reaction in Escherichia coli cells and glycolytic pathway in Saccharomyces cerevisiae cells were utilized as ATP generation systems for glutathione synthetic processes. These two ATP generation systems were well coupled with glutathione synthetase reactions and glutathione was produced by coimmobilized E. coli cells with dextran-bound ATP or by immobilized S. cerevisiae cells. The glycolytic pathway in S. cerevisiae cells was further utilized for the biosynthetic processes of other useful compounds.     

Continuous production of 6-aminopenicillanic acid from penicillin by immobilized microbial cells

Summary For continuous production of 6-aminopenicillanic acid (6-APA) the microbial cells ofEscherichia coli ATCC 9637 having high penicillin amidase (penicillin amidohydrolase, E.C. 3. 5. 1. 11) activity were immobilized by entrapment in a polyacrylamide gel lattice.Enzymatic properties of penicillin amidase of the immobilizedE. coli cells were investigated and compared with those of the intact cells. With regard to optimal pH and temperature, no marked difference was observed. The heat stability was somewhat increased by immobilization of the cells.The enzyme activity of the immobilized cell column was stable, and its half-life was 17 days at 40°C and 42 days at 30°C. From the effluent of the column, 6-APA was easily obtained in a good yield.Abbreviations 6-APA 6-aminopenicillanic acid - BIS N,N-methylenebisacrylamide - DMAPN -dimethylaminopropionitrile - SV space velocity     

Continuous production of thienamycin in immobilized cell systems

A novel 2-L bubble column was used to study the continuous, immobilized cell production of thienamycin. Cells of Streptomyces cattleya were immobilized by culturing them in an appropriate growth medium containing 60/80 mesh celite particles. The dilution rate used during the continuous growth phase was 0.2 h(-1). This growth phase was terminated upon the development of heavy cell films (100-500 mum thickness), and the medium was replaced with an appropriate thienamycin production medium. The system was then operated in a batch mode until thienamycin production began. At that time, continuous feeding of the production medium was initiated and the influence of medium composition and dilution rate on CO(2), NH(4), biomass, and thienamycin production investigated. With synthetic production medium, a doubling of the dilution rate from 0.05 to 0.10 h(-1) resulted in a doubling of the thienamycin volumetric productivity. Rates of CO(2) and NH(4) production increased by ca. factors of three and two, respectively. The rate of PO(4) utilization also doubled. When the dilution rate was decreased to 0.05 h(-1), the rates of CO(2) production and PO(4) utilization quickly decreased (i.e., within 3 h). The rates of NH(4) and thienamycin production also decreased but more slowly (i.e., ca. 100 h after the decrease in dilution rate). With complex production medium, the rates of CO(2) production and PO(4) utilization appeared to be a direct function of dilution rate at the dilution rates tested. Thienamycin production in this case was not a function of dilution rate. Comparing the synthetic medium with the complex medium at either dilution rate, the volumetric rate of thienamycin production was higher in the system being fed complex medium. However, the specific activity (units thienamycin/g cell/h) observed with complex medium was lower than that observed with synthetic medium. The higher volumetric productivity observed with complex medium was the result of a high cell loading. The above observations will be discussed in terms of control of thienamycin synthesis and film thickness effects.     

Electricity production by an overflow-type wetted-wall microbial fuel cell

An overflow-type wetted-wall MFC (WWMFC) was developed to generate a stable voltage from acetate-based substrates. The maximum power density of 18.21 W/m³ was obtained. The power generation showed a saturation-type relationship as a function of initial COD, with a maximum power density (P_max) of 18.82 W/m³ and a saturation constant (K_s) of 227.4 mg/l. Forced air flowing through the cathode chamber had a negligible effect on power generation. Influent flow rate could greatly affect the power generation. The maximum power density was increased by 72.8% when the influent flow rate increased from 5 to 30 ml/min. In addition, increasing ionic strength did not affect the power density and internal resistance. Oxygen could be restrained to diffuse into the anode chamber effectively in the overflow-type WWMFC. And the overflow-type WWMFC could be scaled up conveniently in practical application.     

Propionic acid production in an in situ cell retention bioreactor

Continuous fermentations were conducted with in situ cell retention using spin filters (pore size 5 microm and 10 microm) for propionic acid production by Propionibacterium acidipropionici. Continuous fermentation with a 5-microm pore size spin filter resulted in 50% cell retention. Propionic acid productivity was enhanced (0.9 g l(-1) h(-1)) by approximately four-fold compared to conventional batch fermentation (0.25 g l(-1) h(-1)). The in situ cell retention (5-microm pore size spin filter) bioreactor was operated continuously and smoothly for 8 days at a dilution rate of D=0.05 h(-1).     

Increased power production from a sediment microbial fuel cell with a rotating cathode

The application of a rotating cathode in a river sediment microbial fuel cell increased the oxygen availability to the cathode, and therefore improved the cathode reaction rate, resulting in a higher power production (49 mW/m²) compared to a nonrotating cathode system (29 mW/m²). The increased dissolved oxygen in the water of our lab-scale sediment MFC, however, resulted in a less negative anode potential and a higher anodic charge transfer resistance, which constrained the maximum power density. Thus, an optimum balance between the superior cathode reaction rates and the inferior anode reaction rates due to higher dissolved oxygen levels must be ascertained.     

Electricity production in membrane-less microbial fuel cell fed with livestock organic solid waste

Two different MFC configurations designed for handling solid wastes as a feedstock were evaluated in batch mode: a single compartment combined membrane-electrodes (SCME) design; and a twin-compartment brush-type anode electrodes (TBE) design (reversed T-shape MFC with two-air cathode) without a proton exchange membrane (PEM). Cattle manure was tested as a model livestock organic solid waste feedstock. Under steady conditions, voltage of 0.38 V was recorded with an external resistance of 470 Ω. When digested anaerobic sludge was used as the seed in the SCME design, a maximum power density of 36.6 mW/m² was recorded. When hydrogen-generating bacteria (HGB) were used as the seed used in the TBE design, a higher power density of 67 mW/m² was recorded.     

Immobilization of yeast cells with retention of cell division and extracellular production of macromolecules

Summary Whole cells of a killer strain of Saccharomyces cerevisiae have been covalently linked to the modified hydroxyalkyl methacrylate gel Separon H-1000 E. The occurence of cell division and the killer phenomenon were observed when immobilized cells were incubated in nutrient medium.     

Combining microbial production with chemical upgrading

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Continuous determination of biochemical oxygen demand using microbial fuel cell type biosensor

A mediator-less microbial fuel cell (MFC) was used as a biochemical oxygen demand (BOD) sensor in an amperometric mode for real-time wastewater monitoring. At a hydraulic retention time of 1.05 h, BOD values of up to 100 mg/l were measured based on a linear relationship, while higher BOD values were measured using a lower feeding rate. About 60 min was required to reach a new steady-state current after the MFCs had been fed with different strength artificial wastewaters (Aws). The current generated from the MFCs fed with AW with a BOD of 100 mg/l was compared to determine the repeatability, and the difference was less than 10%. When the MFC was starved, the original current value was regained with a varying recovery time depending on the length of the starvation. During starvation, the MFC generated a background level current, probably due to an endogenous metabolism.     

Inducible cell lysis systems in microbial production of bio-based chemicals

The release of products from microbial cells is an essential process for industrial scale production of bio-based chemicals. However, traditional methods of cell lysis, e.g., mechanical disruption, chemical solvent extraction, and immobilized enzyme degradation, account for a large share of the total production cost. Thus, an efficient cell lysis system is required to lower the cost. This review has focused on our current knowledge of two cell lysis systems, bacteriophage holin–endolysin system, and lipid enzyme hydrolysis system. These systems are controlled by conditionally inducible regulatory apparatus and applied in microbial production of fatty acids and polyhydroxyalkanoates. Moreover, toxin–antitoxin system is also suggested as alternative for its potential applications in cell lysis. Compared with traditional methods of cell disruption, the inducible cell lysis systems are more economically feasible and easier to control and show a promising perspective in industrial production of bio-based chemicals.     

Electricity production from xylose using a mediator-less microbial fuel cell

Electricity generation integrated with xylose degradation was investigated in a two-chamber mediator-less microbial fuel cell (MFC). Voltage output followed saturation kinetics as a function of xylose concentration for concentration below 9.7 mM, with a predicted maximum of 86 mV (6.3 mW m(-2) or 116 mW m(-3)) and half-saturation constant (K(s)) of 0.29 mM. Xylose concentrations from 0.5 mM to 1.5 mM resulted in coulombic efficiencies and maximum voltage ranging from 41+/-1.6% to 36+/-1.2% and 55+/-2.0 mV to 70+/-3.0 mV respectively. Xylose degradation rate increased with increasing xylose concentration up to 9.7 mM and the predicted maximum degradation rate was 0.13 mM h(-1) and K(s) of 3.0 mM. Stirring by nitrogen in the anode chamber led to 99+/-2.3 mV maximum voltage (8.4+/-0.4 mW m(-2) or 153+/-7.1 mW m(-3)) and 5.9+/-0.3% coulombic efficiency at MFC running time 180 h, which were respectively 17+/-1.2% and 37+/-1.8%, higher than those without stirring. The COD removal under stirring was 22.1+/-0.3%, which was slightly lower than that of 23.7+/-0.4% under no stirring. However, stirring resulted in 59% lower xylose degradation rate. This work demonstrates that xylose can be used in the MFC for electricity production. Comparatively higher electricity generation and coulombic efficiency can be obtained by adjusting initial xylose concentration and applying stirring in the anode chamber.     

Mass production of animal cells in nude mice with retention of cell specific markers.

Biochemical analysis of macromolecular constituents of somatic cells in culture frequently requires the production of large quantities of cells from small initial populations, often a laborious and expensive procedure. Here we show that nude mice, because of their genetic immune deficiency, provide a relatively simple and reliable means of growing large quantities of cells irrespective of the species or tissue of origin. Most established animal cell lines are capable of growing as large tumors in these athymic mice. The passage of mammalian cells in nude mice does not cause either the loss or modification of specific biochemical, chromosomal, antigenic or other cellular markers, nor the induction of malignant transformation of the host cells. Tumors formed by the injected cells grow as localized, encapsulated masses, and host cell admixture due to elements of the vascular system in the tumor is variable but not extensive. Pure cultures of the original cell type can easily be recovered from the tumors if they are derived from previously established cell lines. The use of nude mice for large scale growth of animal cells is particularly advantageous for cell lines which are not adapted to mass suspension culture for highly differentiated functional tumor cells which cannot be grown in vitro.     

Continuous power generation and microbial community structure of the anode biofilms in a three-stage microbial fuel cell system

A mediator-less three-stage two-chamber microbial fuel cell (MFC) system was developed and operated continuously for more than 1.5 years to evaluate continuous power generation while treating artificial wastewater containing glucose (10 mM) concurrently. A stable power density of 28 W/m³ was attained with an anode hydraulic retention time of 4.5 h and phosphate buffer as the cathode electrolyte. An overall dissolved organic carbon removal ratio was about 85%, and coulombic efficiency was about 46% in this MFC system. We also analyzed the microbial community structure of anode biofilms in each MFC. Since the environment in each MFC was different due to passing on the products to the next MFC in series, the microbial community structure was different accordingly. The anode biofilm in the first MFC consisted mainly of bacteria belonging to the Gammaproteobacteria, identified as Aeromonas sp., while the Firmicutes dominated the anode biofilms in the second and third MFCs that were mainly fed with acetate. Cyclic voltammetric results supported the presence of a redox compound(s) associated with the anode biofilm matrix, rather than mobile (dissolved) forms, which could be responsible for the electron transfer to the anode. Scanning electron microscopy revealed that the anode biofilms were comprised of morphologically different cells that were firmly attached on the anode surface and interconnected each other with anchor-like filamentous appendages, which might support the results of cyclic voltammetry. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.