Derbal K, Bencheikh-Lehocine M, Cecchi F, Meniai A-H, Pavan P
Laboratoire de l'Ingénierie des Procédés de l'Environnement (LIPE), Département de Chimie Industrielle, Faculté des Sciences de l'Ingénieur, Université Mentouri, Constantine, Algeria.
Bioresour Technol. 2009 Feb;100(4):1539-43. doi: 10.1016/j.biortech.2008.07.064. Epub 2008 Oct 26.
Anaerobic digestion model no. 1 model of international water association was applied to a full scale anaerobic co-digestion process for the treatment of the organic fraction of municipal solid wastes along with activated sludge wastes originating from a municipal wastewater treatment plant. This operation was carried out in a digester of 2000 m(3) in volume. It is operates at an average hydraulic retention time of 26.9 days with an average organic loading rate of 1.01 kg TVS/m(3) day, at a temperature of 37 degrees C with an average gas production rate of 0.296 m(3)/m(3) day. The aim of the present study is to compare the results obtained from the simulation with the experimental values. The simulated results showed a good fit for pH, methane and carbon dioxide percentages, biogas volume, chemical oxygen demand, total volatile fatty acids, inorganic nitrogen and inorganic carbon.
国际水协会的1号厌氧消化模型被应用于一个全尺寸厌氧共消化过程,用于处理城市固体废物的有机部分以及来自城市污水处理厂的活性污泥废物。该操作在一个容积为2000立方米的消化池中进行。其平均水力停留时间为26.9天,平均有机负荷率为1.01千克总挥发性固体/立方米·天,温度为37摄氏度,平均产气率为0.296立方米/立方米·天。本研究的目的是将模拟结果与实验值进行比较。模拟结果表明,在pH值、甲烷和二氧化碳百分比、沼气产量、化学需氧量、总挥发性脂肪酸、无机氮和无机碳方面拟合良好。