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Biohydrogen Production as Clean Fuel from physically Pretreated Mixed Culture

BACKGROUND: Due to depletion of fossil fuel reserves, global warming, and the need for energy efficiency, the new energy resource is required. For this purpose, hydrogen can be considered as clean and efficient energy carrier. In this study, biohydrogen production from physical pretreated mixed cult...

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Detalles Bibliográficos
Autores principales: Fatehizadeh, Ali, Amin, Mohammad Mehdi, Bina, Bijan, Zare, Mohammad Reza, Ghasemian, Mohammad, Taheri, Ensiyeh
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Medknow Publications & Media Pvt Ltd 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5991287/
https://www.ncbi.nlm.nih.gov/pubmed/29930920
http://dx.doi.org/10.4103/2277-9175.233030
Descripción
Sumario:BACKGROUND: Due to depletion of fossil fuel reserves, global warming, and the need for energy efficiency, the new energy resource is required. For this purpose, hydrogen can be considered as clean and efficient energy carrier. In this study, biohydrogen production from physical pretreated mixed culture was investigated. MATERIALS AND METHODS: In this study, the optimal conditions for physical pretreatment of mixed culture were investigated for the enrichment of hydrogen-producing bacteria (HPB). Three individual pretreatment processes, including thermal, ultraviolet (UV) radiation, and ultrasonication (US) were conducted in batch tests. The batch tests were carried out via 500 mL glass flasks with working volume 400 mL. Glucose was used as sole substrate, and other essential nutrient and trace elements were added. To agitation of substrate with HPB inoculum, the magnet stirrer was used at 60 rpm. RESULTS: The results showed the production of H(2) gas could be increased by appropriate pretreatment methods including thermal pretreatment at 100°C. At 100°C as a pretreatment, the volume of H(2) gas was 112.25 mL and followed by US (97.46 mL), UV (89.11 mL), 80°C (72.72 mL), 90°C (53.95 mL), and 70°C (26.01 mL). In the pretreatment methods, the solution pH and effluent soluble chemical oxygen demand was 6.3–6.7 and 5100–8300 mg/L, respectively. CONCLUSIONS: The Gompertz model depicts that all R(2) values were more than 0.93, indicating that the fitted curves were best fitted with the experimental points.