Dissertação

Produção de biogás a partir da digestão anaeróbica de efluentes orgânicos em reator UASB

With the rising demand for renewable energy and environmental protection, anaerobic anaerobic digestion technology for biogas production has attracted considerable attention around the world. Anaerobic digestion is a biological process that converts organic matter into a methane rich gas. It is a we...

ver descrição completa

Autor principal: Tunes, Caroline Ribeiro
Grau: Dissertação
Idioma: pt_BR
Publicado em: Universidade Federal do Tocantins 2017
Assuntos:
Acesso em linha: http://hdl.handle.net/11612/381
Resumo:
With the rising demand for renewable energy and environmental protection, anaerobic anaerobic digestion technology for biogas production has attracted considerable attention around the world. Anaerobic digestion is a biological process that converts organic matter into a methane rich gas. It is a well established technology for the treatment of waste and effluents with high organic content, from industrial processes and domestic activities. In this study, vinasse, a by-product of the sugar and alcohol industry and dairy effluent, a by-product of the dairy industry, were evaluated for biogas production in a UASB reactor. The organic effluents used in this work were collected from large industries located in Brazil and Germany. For the anaerobic digestion of the vinasse and the lactic effluent, a UASB reactor UASB was used in laboratory scale, with a mesophilic temperature and with a capacity of 87 L. For digestion of the vinasse, the UASB reactor operated for 15 days, with COV of 2 Kg COD m-3 d-3 and TDH of 11.5 days. The results obtained in this study showed a good functioning of the UASB reactor applied to vinasse. This study yielded a COD removal efficiency of 71% and an accumulated biogas volume of 1160 liters with a methane concentration of around 48 to 57%. For the digestion of dairy effluent, the UASB reactor operated for 51 days. The efficiency of the reactor from the organic loading rate of 6 kg COD m-3 d-3 and hydraulic holding time (TDH) of 11.8 was studied and its performance was evaluated by monitoring pH, COD, alkalinity ratio FOS / TAC and biogas production. The efficiency of COD removal was observed in 71.3%. The pH of the reactor was verified between 7.0-7.3 and the FOS / TAC value between 0.129-0.152. The average biogas production was observed at 85.8 liters per day, and the specific biogas volume was between 0.46-0.71 L / g COD per day. The methane content in the produced biogas, the maximum and minimum value was observed in 56.6% and 40%, respectively.