Rao M S, Singh S P
Biomass and Waste Management Laboratory, School of Energy and Environmental Studies, Faculty of Engineering Sciences, Devi Ahilya University, Khandwa Road Campus, Indore, MP PIN--452 017, India.
Bioresour Technol. 2004 Nov;95(2):173-85. doi: 10.1016/j.biortech.2004.02.013.
Batch digestion of municipal garbage was carried out for 100 days at room temperature (26+/-4 degrees C; average temperature 25 degrees C) and at ambient temperature (32+/-10 degrees C; average temperature 29 degrees C) conditions for total solids concentrations varying between 45 and 135 g/l. A first order model based on the availability of substrate as the limiting factor was used to perform the kinetic studies of batch anaerobic digestion system. Effect of organic solids concentration and digestion time on biogas yield was studied and mass and energy balance analysis was conducted for batch digestion. The net bioenergy yield from municipal garbage and corresponding bioprocess conversion efficiency over the length of the digestion time were observed to be 12,528 kJ/kg volatile solids and 84.51% respectively. The methane content of the biogas generated from the reactors was in the range of 62-72% with the overall average methane content of the biogas, computed over the total digestion period was 65 vol%.
在室温(26±4℃;平均温度25℃)和环境温度(32±10℃;平均温度29℃)条件下,对总固体浓度在45至135 g/l之间的城市垃圾进行了100天的间歇式消化。基于底物可用性作为限制因素的一级模型用于进行间歇式厌氧消化系统的动力学研究。研究了有机固体浓度和消化时间对沼气产量的影响,并对间歇式消化进行了质量和能量平衡分析。在消化时间内,城市垃圾的净生物能源产量和相应的生物过程转化效率分别为12,528 kJ/kg挥发性固体和84.51%。反应器产生的沼气中甲烷含量在62-72%范围内,在整个消化期间计算得出的沼气总体平均甲烷含量为65 vol%。