Sheng-Shung Cheng

Self-excreted mediator from Escherichia coli K-12 for electron transfer to carbon electrodes.

Escherichia coli K-12 was cultured under anaerobic conditions to form biofilm on carbon fiber electrodes in glucose-containing medium. The anodic current increased with the development of the biofilm and depended on the glucose concentration. Cyclic voltammetric results support the presence of a redox compound(s) excreted from E. coli cells in the biofilm. The compound remained in the film under conditions of continuous flow and gave a couple of oxidation and reduction waves, which may be assigned to a menaquinone-like compound based on the mid-point potential (−0.22xa0V vs Ag|AgCl at pHxa07.1) and its pH dependence. The catalytic current started to increase around the anodic peak potential of the redox compound and also increased by the permeabilization of the E. coli cell membranes with ethylenediamine tetraacetic acid-treatment. The results indicate that the E. coli-excreted redox compound works as a mediator for the electron transfer from the E. coli cells to the electrode as the final electron acceptor. The activity of the redox compound in the E. coli-biofilm as a mediator with some mobility was also verified for diaphorase-catalyzed electrochemical oxidation of NADH.

Effects of oxygen on Shewanella decolorationis NTOU1 electron transfer to carbon-felt electrodes

To clarify the major factor caused by oxygen-enhancing charge production of Shewanella decolorationis NTOU1 towards a polarized anode, a series of experimental runs (i.e., with/without ambient air flushing and with/without ammonia addition as nitrogen source) were conducted in this study. Within 6-day of operation at +0.4 V vs. Ag|AgCl and starting with 35 mM of lactate, consistently the electrical charge production under the aerobic condition was higher than that under the anaerobic condition. In all the experimental runs, the values of nicotinamide adenine dinucleotide (NADH) production were found to be correlated positively and significantly with the charge production, but the highest Coulombic efficiency of 18% was observed under the anaerobic conditions without ammonia addition while the lowest charge production occurred. Those results indicate that NADH production enhanced by oxygen is the leading cause of the increase of the charge production, but the biomass production and the oxygen reduction would both consume NADH electrons and lead to lower electron recoveries. In addition, whether under constant aerobic or anaerobic, or alternating aerobic/anaerobic conditions, chronoamperometric results made it possible to rule out other factors, like lactate uptake rate or cell growth, which might increase the charge production under aerobic conditions. By using high performance liquid chromatography, some diffusive flavins (e.g., 0.5 microM of riboflavin) were found under the aerobic condition, but were not found under the anaerobic one. However, from results of cyclic voltammetry (CV), the signals of flavins were found to be approximately the same under both conditions. Although it is inferred that oxygen renders the flavins secreted extracellularly, that is not the major effect of oxygen for boosting the charge production. Furthermore, bound flavins under anaerobic condition were found to be effectively electrocatalytic according to sigmoidal CV result.

Strategy of controlling the volumetric loading rate to promote hydrogen-production performance in a mesophilic-kitchen-waste fermentor and the microbial ecology analyses.

The kitchen waste was chosen as a high solid (42 gL(-1) of volatile suspended solid, VSS) and high organic (107 gL(-1) of chemical oxygen demand) feedstock for operating a 3-L mesophilic fermentor. The greatest specific hydrogen production rate ( r(H2) was observed in Stage 3 as 3.4 L-H2 L(-1) day(-1) with a volumetric loading rate (VLR) of 100 g-CODL(-1) day(-1); the highest hydrogen yield was observed in Stage 2 as 96 mL-H2 g(-1) of influent VSS with a VLR of 46 g-COD L(-1) day(-1). In Stages 1 (with a VLR of 27 g-COD L(-1)) and 2, the sum of Butyrivibrio fibrisolvens and Clostridium proteoclasticum is dominant, but in Stage 3, Olsenella genomosp, became dominant and constituted 44% of the entire population. The dependence of VLR and r(H2)could be regressed as a linear equation of r(H2) = (2.83 VLR + 40.5) x 10(-2) .

Removal of nitrogen from secondary effluent of a petrochemical industrial park by a hybrid biofilm-carrier reactor with one-stage ANAMMOX

A laboratory study was undertaken to explore the capability of one-stage ANAMMOX in a hybrid biofilm-carrier reactor (HBCR) fed with petrochemical wastewater. Under favorable operating conditions in continuous-flow operations (at the dissolved oxygen level of 0.5-1.0 mg L(-1)), the average total nitrogen (TN) removal efficiency reached 62-67% and approximately 90% of TN can be removed by ANAMMOX. In batch operations of the hybrid biofilm-carrier reactor (without adding carbon substrate), the specific TN removal rate of the reactor in which both Kaldnes and nonwoven carriers were kept was two-fold higher than that of the reactor in which only nonwoven carriers were kept. This indicated that the microbial activity of thinner biofilms (Kaldnes carriers) was remarkably higher than that of thicker biofilms (nonwoven carriers). Finally, based on the 16S rRNA clone library, a cluster of ANAMMOX Candidatus Kuenenia stuttgartiensis was identified.

A combined upflow anaerobic sludge bed, aerobic, and anoxic fixed-bed reactor system for removing tetramethylammonium hydroxide and nitrogen from light-emitting diode wastewater

ABSTRACT A laboratory study using a combined upflow anaerobic sludge bed (UASB) and aerobic and anoxic fixed-bed reactor system was undertaken to explore its capability for removing tetramethylammonium hydroxide (TMAH) and nitrogen from light-emitting diode wastewater. When the organic loading rate was maintained at 0.26–0.65u2005kg TMAHu2005m−3u2005d−1, the UASB reactor removed 70–100% of TMAH through methanogenesis. When the -N loading rate was maintained at 0.73–1.4u2005kg -Nu2005m−3u2005d−1, the aerobic reactor oxidized 31–59% of -N to -N through nitritation. When the nitrogen loading rate was maintained at 0.42–0.75u2005kgu2005Nu2005m−3u2005d−1, the anoxic reactor removed 27–63% of nitrogen through anammox. The performance data of the combined reactor system agreed well with the stoichiometric relationships of methanogenesis, nitritation, and anammox. The batch studies showed that a higher initial TMAH concentration of up to 2520u2005mgu2005L−1 gave a higher methanogenic activity of up to 16u2005mL CH4u2005g−1 VSSu2005d−1. An increase in the initial TMAH concentration of up to 500u2005mgu2005L−1 gradually decreased the activity of ammonia-oxidizing bacteria; whereas an increase in the initial TMAH concentration of up to 47u2005mgu2005L−1 imposed a marked inhibiting effect on the activity of anammox bacteria.

WITHDRAWN: Bioaugmentation strategies to improve cellulolytic and hydrogen-producing characteristics of CSTR intermittent fed with vegetable kitchen waste and napiergrass

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