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采用两级厌氧消化处理玉米乙醇蒸馏废水。

Treatment of corn ethanol distillery wastewater using two-stage anaerobic digestion.

作者信息

Ráduly B, Gyenge L, Szilveszter Sz, Kedves A, Crognale S

机构信息

Department of Bioengineering, Sapientia Hungarian University of Transylvania, Pta. Libertatii 1, 530104 M-Ciuc, Romania E-mail:

DIBAF, University of Tuscia, Via S. Camillo de Lellis, 01100 Viterbo, Italy.

出版信息

Water Sci Technol. 2016;74(2):431-7. doi: 10.2166/wst.2016.185.

DOI:10.2166/wst.2016.185
PMID:27438248
Abstract

In this study the mesophilic two-stage anaerobic digestion (AD) of corn bioethanol distillery wastewater is investigated in laboratory-scale reactors. Two-stage AD technology separates the different sub-processes of the AD in two distinct reactors, enabling the use of optimal conditions for the different microbial consortia involved in the different process phases, and thus allowing for higher applicable organic loading rates (OLRs), shorter hydraulic retention times (HRTs) and better conversion rates of the organic matter, as well as higher methane content of the produced biogas. In our experiments the reactors have been operated in semi-continuous phase-separated mode. A specific methane production of 1,092 mL/(L·d) has been reached at an OLR of 6.5 g TCOD/(L·d) (TCOD: total chemical oxygen demand) and a total HRT of 21 days (5.7 days in the first-stage, and 15.3 days in the second-stage reactor). Nonetheless the methane concentration in the second-stage reactor was very high (78.9%); the two-stage AD outperformed the reference single-stage AD (conducted at the same reactor loading rate and retention time) by only a small margin in terms of volumetric methane production rate. This makes questionable whether the higher methane content of the biogas counterbalances the added complexity of the two-stage digestion.

摘要

在本研究中,在实验室规模的反应器中对玉米生物乙醇蒸馏废水的中温两段式厌氧消化(AD)进行了研究。两段式厌氧消化技术在两个不同的反应器中分离厌氧消化的不同子过程,从而能够为不同工艺阶段涉及的不同微生物群落使用最佳条件,进而允许更高的适用有机负荷率(OLR)、更短的水力停留时间(HRT)和更好的有机物转化率,以及所产生沼气中更高的甲烷含量。在我们的实验中,反应器以半连续相分离模式运行。在有机负荷率为6.5 g TCOD/(L·d)(TCOD:总化学需氧量)和总水力停留时间为21天(第一阶段为5.7天,第二阶段反应器为15.3天)的条件下,达到了1092 mL/(L·d)的特定甲烷产量。尽管如此,第二阶段反应器中的甲烷浓度非常高(78.9%);就体积甲烷生产率而言,两段式厌氧消化仅比参考单段式厌氧消化(在相同的反应器负荷率和停留时间下进行)略胜一筹。这使得沼气中较高的甲烷含量是否能抵消两段式消化增加的复杂性令人质疑。

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