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采用集成式转鼓和厌氧分相固体消化器系统从城市固体废物中生产沼气。

Biogas production from municipal solid wastes using an integrated rotary drum and anaerobic-phased solids digester system.

机构信息

Department of Biological and Agricultural Engineering, University of California, Davis, CA 95616, USA.

出版信息

Bioresour Technol. 2010 Aug;101(16):6374-80. doi: 10.1016/j.biortech.2010.03.075. Epub 2010 Apr 20.

DOI:10.1016/j.biortech.2010.03.075
PMID:20409703
Abstract

This research was conducted to develop an integrated rotary drum reactor (RDR)-anaerobic-phased solids (APS) digester system for the treatment of municipal solid waste (MSW) to produce biogas energy and achieve waste reduction. A commercial RDR facility was used to provide a 3-d pretreatment and sufficient separation of the organics from MSW and then the organics were digested in a laboratory APS-digester system for biogas production. The organics generated from the RDR contained 50% total solids (TS) and 36% volatile solids (VS) on wet basis. The APS-digester was started at an organic loading rate (OLR) of 3.1 gVS L(-1) d(-1) and operated at three higher OLRs of 4.6, 7.7 and 9.2 gVS L(-1) d(-1). At the OLR of 9.2 gVS L(-1) d(-1) the system biogas production rate was 3.5 L L(-1) d(-1) and the biogas and methane yields were 0.38 and 0.19 L gVS(-1), respectively. Anaerobic digestion resulted in 38% TS reduction and 53% VS reduction in the organic solids. It was found that the total VFA concentration reached a peak value of 15,000 mg L(-1) as acetic acid in the first 3d of batch digestion and later decreased to about 500 mg L(-1). The APS-digester system remained stable at each OLRs for over 100d with the pH in the hydrolysis reactors in the range of 7.3-7.8 and the pH in the biogasification reactor in 7.9-8.1. The residual solids after the digestion had a high heating value of 14.7 kJ gTS(-1).

摘要

这项研究旨在开发一种集成式转鼓式反应器(RDR)-厌氧分相固体(APS)消化器系统,用于处理城市固体废物(MSW)以生产沼气能源并实现废物减量化。使用商业 RDR 设施对 MSW 进行 3d 预处理并充分分离有机物,然后将有机物在实验室 APS 消化器系统中进行消化以生产沼气。RDR 产生的有机物在湿基上含有 50%总固体(TS)和 36%挥发性固体(VS)。APS 消化器以 3.1 gVS L(-1) d(-1)的有机负荷率(OLR)启动,并在三个更高的 OLR 下运行,分别为 4.6、7.7 和 9.2 gVS L(-1) d(-1)。在 OLR 为 9.2 gVS L(-1) d(-1)时,系统沼气产率为 3.5 L L(-1) d(-1),沼气和甲烷产率分别为 0.38 和 0.19 L gVS(-1)。厌氧消化导致有机固体的 TS 减少 38%,VS 减少 53%。研究发现,在批式消化的前 3d 内,总 VFA 浓度达到 15000mg L(-1),以乙酸计,随后降至约 500mg L(-1)。在每个 OLR 下,APS 消化器系统在超过 100d 内保持稳定,水解反应器中的 pH 值在 7.3-7.8 之间,沼气化反应器中的 pH 值在 7.9-8.1 之间。消化后的剩余固体具有 14.7kJ gTS(-1)的高热值。

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