Start-up of a multi-stage system for biogas production and solid waste treatment in low-tech countries

2003 ◽  
Vol 48 (4) ◽  
pp. 239-243 ◽  
Author(s):  
E.M. Biey ◽  
E.D. Musibono ◽  
W. Verstraete

Vegetable fruit garden wastes were treated anaerobically using a multistage Dranco system. The digesters were composed of three 50 L vessels kept in mesophilic conditions. They were operating at 14.5-17% TS. By controlling the pH in the system, the start-up for biogas production was shortened to 60 days. The pH correction was a buffering which enhanced methanogenic activity in the digesters. With a loading rate of 4.1 kg VS/m3reactor.day, the production of biogas was 5 m3/m3reactor.day, and 60-70% methane content. This allowed making a multisystem by starting every 3 weeks with new vessels in order to maintain biogas production, to be used in industries or in local communities in low-tech countries. The designed model was started in Kinshasa (Congo) where a project is expected to treat one ton of solid waste on a daily basis, for a production of 100 m3 biogas. This cost effectiveness of the system is demonstrated and presents the opportunity for biowaste treatment coupled with environmental protection and substantial energy recovery.

2019 ◽  
Vol 276 ◽  
pp. 06016
Author(s):  
Slamet Raharjo ◽  
Puti S. Komala ◽  
Adjar Pratoto

Current practice in Indonesia shows that Household Solid Waste (HSW) is handled by transferring to landfill site. Meanwhile, around 68% of HSW is composed of biodegradable components, which has potential for biogas production. The current study compares some commercial activators including Green Phosko (GP7) and Effective microorganisms 4 (EM4) with homemade activator in 200 L anaerobic digester equipped with manual mixing for processing kitchen waste (KW). pH and ratio of solid waste to water were set at 8 and 1:2, respectively. Batch experiments show that digester #3 with homemade activator shows superior performance compared to commercial activators. Meanwhile, the digesters with commercial activators show better performance compared to digester control (without activator). Digester #3 produces 1.35 L CH4/kg total solid (TS) and 1.14 L CH4/kg volatile solid (VS). Current work suggests that the homemade activator has the most suitable methanogen bacterium compared to the commercial activators.


2009 ◽  
Vol 29 (2) ◽  
pp. 704-711 ◽  
Author(s):  
Claudia Johanna Sandoval Lozano ◽  
Marisol Vergara Mendoza ◽  
Mariela Carreño de Arango ◽  
Edgar Fernando Castillo Monroy

2016 ◽  
Vol 2 (05) ◽  
pp. 312-320
Author(s):  
Mohammad Asaduzzaman ◽  
June-ichiro Giorgos Tsutsumi ◽  
Ryo Nakamatsu ◽  
Shokory Jamal Abdul Naser

Work ◽  
2018 ◽  
Vol 60 (4) ◽  
pp. 613-622 ◽  
Author(s):  
Juan Carlos Rubio-Romero ◽  
Sebastian Molinillo ◽  
Antonio López-Arquillos ◽  
Rafael Arjona-Jiménez ◽  
José María De La Varga-Salto

2019 ◽  
Vol 57 ◽  
pp. 20-29 ◽  
Author(s):  
Manoj Govind Kharat ◽  
Shankar Murthy ◽  
Sheetal Jaisingh Kamble ◽  
Rakesh D. Raut ◽  
Sachin S. Kamble ◽  
...  

2019 ◽  
pp. 1-16
Author(s):  
Quan Wang ◽  
Xiuna Ren ◽  
Junchao Zhao ◽  
Hongyu Chen ◽  
Meijing Wang ◽  
...  

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