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Hilkiah lgoni, A., Ayotamuno, M.J., Eze, C.L., Ogaji, S.O.T., Probert, S.D., 2008. Designs of anaerobic digesters
for producing biogas from municipal solid-waste. Appl. Energ. 85, 430-438.
Kaparaju, P.L.N., Rintala, J.A., 2006. Thermophilic anaerobic digestion of industrial orange waste. Environ.
Technol. 27, 623-633.
MetCalf, Eddy, 2004. Wastewater Engineering Treatment and Reuse, third ed. McGraw-Hill Inc., New York.
Rasi, S., Veijanen, A., Rintala, J., 2007. Trace compounds of biogas from different biogas production plants.
Energy 32, 1375–1380.
Themelis, N.J., Ulloa, P.A., 2007. Methane generation in landfills. Renewable Energy. 32, 1243-1257.