Genetic Identification of the Bioanode and Biocathode of a Microbial
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Revista Mexicana de Ingeniería Química Vol. 13, No.CONTENIDO 2 (2014) 573-581 Volumen 8, número 3, 2009 / Volume 8, number 3, 2009 GENETIC IDENTIFICATION OF THE BIOANODE AND BIOCATHODE OF A MICROBIAL ELECTROLYSIS CELL 213 Derivation and application of the Stefan-Maxwell equations IDENTIFICACION´ GENETICA´ DEL BIOANODO´ Y BIOCATODO´ DE UNA CELDA (DesarrolloDE y aplicación ELECTROLISIS de las ecuaciones de Stefan-Maxwell) MICROBIANA Stephen Whitaker R. Valdez-Ojeda 1∗, M. Aguilar-Espinosa2, L. Gomez-Roque´ 1, B. Canto-Canche´3, RM. Escobedo 2 1 BiotecnologíaGracia-Medrano / Biotechnology, J. Dom´ınguez-Maldonado, L. Alzate-Gaviria 1Unidad de Energ´ıaRenovable.245 Modelado Centro de la biodegradación de Investigaci´onCient´ıficade en biorreactores de lodos Yucat´an.(CICY).de hidrocarburos totales M´erida,Yucat´an.Calledel petróleo 43 intemperizadosNo. 130,Col. en suelos Chuburn´ade y sedimentos Hidalgo, C.P. 97200. M´exico. 2Unidad de Bioqu´ımicay Biolog´ıaMolecular de Plantas. (Biodegradation modeling of sludge bioreactors of total petroleum hydrocarbons weathering in soil 2Unidad de Biotecnolog´ıa. and sediments) ReceivedS.A. Medina-Moreno, September S. Huerta-Ochoa, 4, 2013; C.A. Accepted Lucho-Constantino, December L. Aguilera-Vázquez, 31, 2013 A. Jiménez- González y M. Gutiérrez-Rojas Abstract 259 Crecimiento, sobrevivencia y adaptación de Bifidobacterium infantis a condiciones ácidas The aim of this study was to identify the microorganisms present on the graphite cloth of the bioanode and biocathode of a Microbial Electrolysis Cell (MEC)(Growth, using survival 16S and ribosomaladaptation of Bifidobacterium RNA gene cloning infantis to and acidic sequencing. conditions) The results obtained indicated that the bioanode clones wereL. related Mayorga-Reyes, with the P. phyla: Bustamante-Camilo,Firmicutes A.(15.3%), Gutiérrez-Nava,Proteobacteria E. Barranco-Florido(7.6%), y BacteroidetesA. Azaola- (30.7%), and Ignavibacteriae (7.6%). Conversely,Espinosa the biocathode clones were related with the phylum Proteobacteria (38.4%). The bioanode clones were related with species265 Statistical identified approach previously to optimization in MECs of andethanol Microbial fermentation Fuel by CellsSaccharomyces (MFCs). cerevisiae However, in the biocathode clones were related with Rhodopseudomonaspresence of palustrisValfor® zeolite, which NaA have not been reported for hydrogen production by MEC. R. palustris 3 3 probably should be involved into(Optimización hydrogen estadística production de la of fermentación 0.011 m etanólicaH2/m decathode Saccharomyces liquid cerevisiae volume en per presencia day with de an applied voltage of 1 V. zeolita Valfor® zeolite NaA) Keywords: exoelectrogenic bacteria,G. Inei-Shizukawa, hydrogen H. generation, A. Velasco-Bedrán,Rhodopseudomonas G. F. Gutiérrez-López palustris and H. Hernández-Sánchez, hydrogenase, MEC. Resumen Ingeniería de procesos / Process engineering El objetivo de este trabajo fue la identificacion´ de microorganismos presentes en la tela de grafito del biocatodo´ y bioanodo´ 271 Localización de una planta industrial: Revisión crítica y adecuación de los criterios empleados en de una Celda de Electrolisis´ Microbiana (CEM), utilizando clonacion´ y secuenciacion´ del gen 16S del RNA ribosomal. Los esta decisión resultados obtenidos indicaron que las clonas del bioanodo´ se relacionaron con los filos Firmicutes (15.3%), Proteobacteria (Plant site selection: Critical review and adequation criteria used in this decision) (7.6%), Bacteroidetes (30.7%), and Ignavibacteriae (7.6%). Mientras que las clonas del biocatodo´ se relacionaron con el filo J.R. Medina, R.L. Romero y G.A. Pérez Proteobacteria (38.4%). Las clonas del bioanodo´ se relacionaron con especies identificadas previamente en CEM y Celdas de Combustible Microbiana (CCM). Sin embargo, las clonas del biocatodo´ se relacionaron con Rhodopseudomonas palustris, la cual no hab´ıa sido reportada para la produccion´ de hidrogeno´ a traves´ de CEM. Los resultados sugieren la participacion´ de esta especie en la produccion´ de 0.011 m3 H /m3 por volumen l´ıquido de catodo´ al d´ıa aplicando un voltaje de 1. 2 Palabras clave: bacteria exoelectrogenica,´ generacion´ de hidrogeno,´ Rhodopseodomonas palustris, hidrogenasa, CEM. 1 Introduction Microbial reactors have opened up new 2007), by their beneficial to environment into using possibilities and are attracting a lot of attention waste waters (Dom´ınguez-Maldonado et al., 2014). for producing electricity with Microbial Fuel Cells (MFCs) (Logan and Regan, 2006) and hydrogen with Hydrogen production with MECs involves Microbial Electrolysis Cells (MECs) (Rozendal et al., separating the anode and cathode compartments with an ion exchange membrane, and connecting them ∗Corresponding author. E-mail: [email protected] Tel. (52)999- 942-83-30, Fax (52) 999-981-39-00 Publicado por la Academia Mexicana de Investigacion´ y Docencia en Ingenier´ıa Qu´ımica A.C. 573 Valdez-Ojeda et al./ Revista Mexicana deIngenier ´ıaQu ´ımica Vol. 13, No. 2 (2014) 573-581 via an external electrical circuit (Rozendal et al., 2 Methodology 2007). At the anode (also called the bioanode), microorganisms oxidize organic compounds, 2.1 Microbial Electrolysis Cell (MEC) transferring electrons by direct contact between the bacterial cell and electrode (nanowires or membrane- A double-chamber MEC system was constructed bound c-type cytochrome) or by intermediate from poly-(methyl-methacrylate) with an operational electron carrier molecules (endogenous or exogenous) volume of 0.57 L, and the chambers were separated 2 (Alfonta, 2010). The electrons are conducted by the by Nafion® 117 (22.2 cm ). The electrodes were 2 external circuit to the cathode to generate H2 through graphite cloth (32 cm ), connected by an external the reduction of H+ ions (Drapcho et al., 2008). circuit with stainless steel and covered with termofit® However, bacterial cells possess energetic limitations (Chae et al. 2008). System startup and operation were to complete the oxidation of organic substrates for carried out in accordance with Rozendal et al. (2007) hydrogen formation, requiring the application of an and Jeremiasse et al. (2010). additional voltage to convert organic substrate to CO2 and hydrogen (Geelhoed et al., 2010; Liu et al., 2010). 2.2 Biocathode startup The hydrogen production reaction can be This electrode is referred to as the bioelectrode (during catalyzed using platinum (Rozendal et al., 2007), biocathode startup) or biocathode (after biocathode but its high cost limits scale-up (Liu et al., 2010). startup). The bioelectrode chamber was inoculated Furthermore, its susceptibility to poisoning has with a mixed culture of microorganisms. The led researchers to examine non-precious metals composition of inoculums was soil (30 g/L), cow (Selembo et al., 2010) and other alternatives. In manure (300 g/L), pig manure (150 g/L), Na2CO3 (1.5 this regard, purified hydrogenase enzymes isolated g/L), commercial sucrose (5 g/L), and tap water. The from microorganisms have been used to replace inoculum was pretreated to eliminate methanogenic chemical catalysts in MFCs, because they catalyze microorganisms. This consisted of thermal treatment + − the reversible H2 ! 2H + 2e reaction (Lojou at 100 ºC for 15 min (Logan et al., 2008). et al., 2011). Nevertheless, whole immobilized The bioelectrode was inoculated and subjected to cells of Desulfovibrio vulgaris (well known for a three-phase biocathode startup as follows. After its hydrogenase activity) have demonstrated more inoculation, the bioelectrode was started up as a stable and maintained catalytic activity for hydrogen bioanode. This occurred in phase 1, which meant production than enzyme immobilization (Lojou et al., that the bioelectrode chamber was initially operated 2002). in batch mode to allow the microorganisms to adapt to the bioelectrode chamber without being washed Likewise, biocathodes have been conceived that out immediately. During this phase, 15 mM sodium consist of microorganisms covering an electrode made acetate was used as the carbon source. After 63 hrs, of material (e.g., carbon) or dispersed in the electrolyte anodic current generation started and operation was to catalyze cathodic reactions in MECs (Rabaey and switched from batch to continuous mode. At this point Rozendal, 2010). The biocathode activity in a MEC of phase 1, the headspace chamber was flushed with therefore depends on the microorganisms’ ability to H2 gas (20 L of metal hydride, 40 mL/min) to achieve take up electrons from the electrode material and H2 saturation. use them to produce hydrogen (Croese et al., 2011). In the transition from phases 2 to 3, a The microorganisms active on the biocathode have polarity reversal scan was performed to determine scarcely been researched for hydrogen production in the suitable bioelectrode potential for biocathode MECs. In this regard, Croese et al. (2011) identified operation. During this scan, the bioelectrode potential Desulfovibrio vulgaris as a dominant ribotype in the was lowered from -0.2 to -0.8 V at a scan rate of 0.025 biocathode of a MEC, but this is the only report so far. mV/s using a potentiostat (Potentiostat, Biologic). The challenge lies in biocathode identification in order At this point, H2 gas flushing was stopped and the to further contribute to knowledge about the reduction carbon source was replaced with sodium bicarbonate process. The aim of this study was to identify the (10 mM) every 24 hrs. The theoretical potential of microorganisms present on the