Department of Chemical Engineering, Govt. Engineering College, Thrissur, Kerala 680 009, India.
Division of Safety & Fire Engineering, School of Engineering, Cochin University of Science and Technology, Cochin, Kerala 682 022, India.
Waste Manag. 2015 Feb;36:93-7. doi: 10.1016/j.wasman.2014.09.024. Epub 2014 Oct 18.
Anaerobic digestion (AD) of the organic fraction of municipal solid waste (OFMSW) is promoted as an energy source and waste disposal. In this study semi dry anaerobic digestion of organic solid wastes was conducted for 45 days in a lab-scale batch experiment for total solid concentration of 100g/L for investigating the start-up performances under thermophilic condition (50 °C). The performance of the reactor was evaluated by measuring the daily biogas production and calculating the degradation of total solids and the total volatile solids. The biogas yield at the end of the digestion was 52.9L/kg VS (volatile solid) for the total solid (TS) concentration of 100g/L. About 66.7% of the volatile solid degradation was obtained during the digestion. 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. The value of reaction rate constant, k, obtained was 0.0249 day(-1).
厌氧消化(AD)有机固体废物(OFMSW)被作为一种能源和废物处理方式而受到推广。在这项研究中,在实验室规模的批式实验中,以总固体浓度为 100g/L 进行了半干厌氧消化有机固体废物,以在 50°C 的高温条件下考察启动性能。通过测量每日沼气产量和计算总固体和总挥发性固体的降解来评估反应器的性能。对于总固体(TS)浓度为 100g/L,沼气产率在消化结束时为 52.9L/kgVS(挥发性固体)。在消化过程中,约 66.7%的挥发性固体得到了降解。基于基质可用性作为限制因素的一阶模型用于进行批量厌氧消化系统的动力学研究。获得的反应速率常数 k 值为 0.0249 天(-1)。