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比较共消化和消化液回流在连续两相厌氧发酵系统中生物氢气和生物甲烷生产性能。

Comparison of bio-hydrogen and bio-methane production performance in continuous two-phase anaerobic fermentation system between co-digestion and digestate recirculation.

机构信息

Institute of Agricultural Engineering, Huanghe Science and Technology University, Zhengzhou 450063, China.

Collaborative Innovation Center of Biomass Energy, Henan Province, Henan Agricultural University, Zhengzhou 450002, China.

出版信息

Bioresour Technol. 2020 Dec;318:124269. doi: 10.1016/j.biortech.2020.124269. Epub 2020 Oct 16.

Abstract

The effect of co-digestion of food waste (FW) and cow dung (CD) with different ratios, and digestate recirculation with different recirculation ratios (RR) on the substrate degradation and energy production in continuous two-stage anaerobic fermentation system was investigated. Results from experiments indicated that co-digestion and digestate recirculation could promote the hydrogen production rate (HPR) and the methane production rate (MPR). Maximum HPR and MPR of 3.3 and 3.1 L/L/d were achieved for two-stage fermentation with recirculation system at RR of 0.4. Meanwhile, both co-digestion and digestate recirculation technology could reduce the amount of alkali addition to maintain pH in the hydrogen-reactor. Compared to digestate recirculation, co-digestion of FW and CD promote much more energy production, 654.9 and 4854.8 kJ/kgVSr were obtained from the co-digestion of FW and CD with the ratio of 2:1 in the hydrogen reactor and the methane reactor.

摘要

考察了不同比例的食物垃圾(FW)和牛粪(CD)共消化,以及不同循环比(RR)的消化液回流对连续两段式厌氧发酵系统中基质降解和能量产生的影响。实验结果表明,共消化和消化液回流可以提高产氢率(HPR)和产甲烷率(MPR)。在 RR 为 0.4 的回流系统下,两段式发酵的最大 HPR 和 MPR 分别达到 3.3 和 3.1 L/L/d。同时,共消化和消化液回流技术均可减少碱的添加量,以维持氢反应器中的 pH 值。与消化液回流相比,FW 和 CD 的共消化更能促进能量产生,在氢反应器和甲烷反应器中,FW 和 CD 的比例为 2:1 时,共消化可分别获得 654.9 和 4854.8 kJ/kgVSr。

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