Department of Civil, Environmental and Materials Engineering (DICAM), Faculty of Engineering, University of Bologna, via Terracini 28, 40131 Bologna, Italy.
Water Res. 2012 Feb 1;46(2):413-24. doi: 10.1016/j.watres.2011.11.001. Epub 2011 Nov 11.
An effective mesophilic continuous anaerobic digestion process fed only with a mechanically sorted organic fraction of municipal solid waste (MS-OFMSW) was developed. During a preliminary 3-month experimental phase, the microbial consortium was acclimated toward MS-OFMSW by initially filling the reactor with cattle manure and then continuously feeding it with MS-OFMSW. The Hydraulic Retention Time (HRT) and Organic Loading Rate (OLR) were 23 days and 2.5 g/L/day, respectively. After 4 weeks, the reactor reached stationary performances (84% COD removal yield, 0.15 L(CH₄)/g(COD removed) methane production yield). The acclimated consortium was then employed in a second run in which the reactor was operated under steady state conditions at the previous HRT and OLR for 73 days. The COD removal and the methane production yield increased up to 87% and 0.25 L(CH₄) /g(CODremoved), respectively. The capability of the acclimated consortium to biomethanize MS-OFMSW was further studied via batch digestion experiments, carried out by inoculating the target waste with reactor effluents collected at the beginning of first run and at the end of the first and second run. The best normalized methane production (0.39 L(CH₄) /g(initial COD)) was obtained with the inoculum collected at the end of the second run. Molecular analysis of the microbial community occurring in the reactor during the two sequential runs indicated that the progressive improvement of the process performances was closely related to the selection and enrichment of specific hydrolytic and acidogenic bacteria in the reactor.
开发了一种仅以机械分拣的城市固体废物有机部分(MS-OFMSW)为食的高效中温连续厌氧消化工艺。在初步的 3 个月实验阶段,通过最初用牛粪填充反应器,然后连续用 MS-OFMSW 进料,使微生物群落适应 MS-OFMSW。水力停留时间(HRT)和有机负荷率(OLR)分别为 23 天和 2.5 g/L/天。4 周后,反应器达到稳定性能(COD 去除率为 84%,甲烷产率为 0.15 L(CH₄)/g(COD 去除))。然后,将适应的生物群用于第二次运行,在先前的 HRT 和 OLR 下在稳定状态下操作反应器 73 天。COD 去除率和甲烷产率分别提高到 87%和 0.25 L(CH₄)/g(COD 去除)。通过接种在第一个运行开始时和第一个和第二个运行结束时从反应器流出物中收集的目标废物,进行分批消化实验,进一步研究了适应的生物群将 MS-OFMSW 生物甲烷化的能力。用第二个运行结束时收集的接种物获得了最佳的归一化甲烷产量(0.39 L(CH₄)/g(初始 COD))。在两个连续运行期间在反应器中发生的微生物群落的分子分析表明,工艺性能的逐步提高与反应器中特定水解和产酸细菌的选择和富集密切相关。