Clean fuels from municipal solid waste for fuel cell buses in metropolitan areas

1996 ◽  
Vol 17 (4) ◽  
pp. 273-298 ◽  
Author(s):  
Eric D. Larson ◽  
Ernst Worrell ◽  
Jeffrey S. Chen
Keyword(s):  
Fuel Cell ◽  
Municipal Solid Waste ◽  
Solid Waste ◽  
Metropolitan Areas ◽  
Clean Fuels

Biogas from the organic fraction of municipal solid waste: Dealing with contaminants for a solid oxide fuel cell energy generator

2014 ◽  
Vol 34 (11) ◽  
pp. 2047-2056 ◽  
Author(s):  
Davide Papurello ◽  
Andrea Lanzini ◽  
Pierluigi Leone ◽  
Massimo Santarelli ◽  
Silvia Silvestri
Keyword(s):  
Fuel Cell ◽  
Municipal Solid Waste ◽  
Solid Oxide Fuel Cell ◽  
Solid Waste ◽  
Solid Oxide ◽  
Oxide Fuel ◽  
Organic Fraction ◽  
Cell Energy

scholarly journals Solid Oxide Fuel Cell Using Municipal Solid Waste Directly as Fuel: Biomass, Resin, Plastic, and Food Waste

2021 ◽  
Vol 9 (8) ◽  
pp. 3124-3136
Author(s):  
Takashi Hibino ◽  
Kazuyo Kobayashi ◽  
Shinya Teranishi ◽  
Takuma Hitomi
Keyword(s):  
Fuel Cell ◽  
Municipal Solid Waste ◽  
Solid Oxide Fuel Cell ◽  
Solid Waste ◽  
Food Waste ◽  
Solid Oxide ◽  
Oxide Fuel

Municipal Solid Waste Leachate Treatment Using Microbial Fuel Cell

2012 ◽  
Vol 610-613 ◽  
pp. 2361-2366
Author(s):  
Li Fang Deng ◽  
Hao Ran Yuan ◽  
Hong Yu Huang ◽  
Yong Chen
Keyword(s):  
Fuel Cell ◽  
Municipal Solid Waste ◽  
Solid Waste ◽  
Microbial Fuel Cell ◽  
Organic Pollutant ◽  
Ammonia Nitrogen ◽  
High Concentration ◽  
Leachate Treatment ◽  
Anode Carbon ◽  
Waste Leachate

Leachate is a high concentration organic wastewater, and microbial fuel cell (MFC) is capable of decomposing and treating organic pollutants directly. Single-chamber MFC using landfill leachate as anolyte was built to get rid of BOD and ammonia-nitrogen organic pollutant in leachate. The use of MFC led to the treatment of the biodegradable organic pollutant of municipal solid waste leachate and the production of electricity. The biofilm was detected on the MFC anode carbon felt, the voltage and power output were achieved 292.7± 5 mV and 2375.1mW.m-2. The suitable running time was about 10 days, when the BOD and ammonia-nitrogen removal efficiencies were achieved about 93.0% and 84.1 %, respectively.

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