کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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1281623 | 1497657 | 2008 | 11 صفحه PDF | دانلود رایگان |

Feasibility of integrating acidogenic and methanogenic processes for simultaneous production of biohydrogen (H2) and methane (CH4) was studied in two separate biofilm reactors from wastewater treatment. Acidogenic bioreactor (acidogenic sequencing batch biofilm reactor, AcSBBR) was operated with designed synthetic wastewater [organic loading rate (OLR) 4.75 kg COD/m3-day] under acidophilic conditions (pH 6.0) using selectively enriched acidogenic mixed consortia. The resultant outlet from AcSBBR composed of fermentative soluble intermediates (with residual carbon source), was used as feed for subsequent methanogenic bioreactor (methanogenic/anaerobic sequencing batch biofilm reactor, AnSBBR, pH 7.0) to generate additional biogas (CH4) utilizing residual organic composition employing anaerobic mixed consortia. During the stabilized phase of operation (after 60 days) AcSBBR showed H2 production of 16.91 mmol/day in association with COD removal efficiency of 36.56% (SDRA—1.736 kg COD/m3-day). AnSBBR showed additional COD removal efficiency of 54.44% (SDRM—1.071 kg COD/m3-day) along with CH4 generation. Integration of the acidogenic and methanogenic processes enhanced substrate degradation efficiency (SDRT—4.01 kg COD/m3-day) along with generation of both H2 and CH4 indicating sustainability of the process.
Journal: International Journal of Hydrogen Energy - Volume 33, Issue 9, May 2008, Pages 2156–2166