Bolzonella D, Pavan P, Mace S, Cecchi F
Department of Science and Technology, University of Verona. Strada Le Grazie,15-37134 Verona, Italy.
Water Sci Technol. 2006;53(8):23-32. doi: 10.2166/wst.2006.232.
This paper presents a comparison of dry anaerobic digestion reactors fed with differently sorted municipal organic solid wastes. One reactor was fed with source sorted organic wastes and a second reactor was fed with mixed organic wastes consisting of grey wastes, mechanically selected municipal solid wastes and sludge. The two reactors utilised the same process (Valorga) and operational conditions at full scale. The results of the study emphasise the influence of the kind of treated material on the process performances, especially in terms of biogas and methane production, thus, energy reclamation. The reactor treating the source sorted organic waste and the reactor treating the mixed organic wastes generated some 200 m3 and 60 m3 of biogas per ton of waste treated, respectively, while the specific methane production was some 0.40 and 0.13 m3CH4/kgTVS, respectively. The mass balance and the final fate of the digested material from the two reactors were also clearly different. As for the costs, these were some 29 Euro per ton of treated waste (50% for personnel) and 53 Euro/ton for disposing of the rejected materials. Incomes were some 100 Euro/ton (on average) and an other 15 Euro/ton came from green certificates. The initial investment was 16 million Euros.
本文介绍了以不同分类的城市有机固体废物为原料的干式厌氧消化反应器的比较情况。一个反应器采用源头分类的有机废物作为原料,另一个反应器采用由灰色废物、机械分选的城市固体废物和污泥组成的混合有机废物作为原料。这两个反应器在全规模下采用相同的工艺(瓦洛加工艺)和运行条件。研究结果强调了所处理物料种类对工艺性能的影响,特别是在沼气和甲烷产量方面,进而在能源回收方面的影响。处理源头分类有机废物的反应器和处理混合有机废物的反应器,每吨处理废物分别产生约200立方米和60立方米的沼气,而单位甲烷产量分别约为0.40立方米CH₄/千克总挥发性固体和0.13立方米CH₄/千克总挥发性固体。两个反应器消化后物料的质量平衡和最终去向也明显不同。至于成本,处理每吨废物约为29欧元(人员成本占50%),处置废弃物料的成本为53欧元/吨。收入约为100欧元/吨(平均),另外还有15欧元/吨来自绿色证书。初始投资为1600万欧元。