A new method of two-phase anaerobic digestion for fruit and vegetable waste treatment. (July 2016)

• Record Type: Journal Article
• Authors: Wu, Yuanyuan; Wang, Cuiping; Liu, Xiaoji; Ma, Hailing; Wu, Jing; Zuo, Jiane; Wang, Kaijun
• Is Part Of: Bioresource technology. Volume 211(2016)
• Page Start: 16
• Page End: 23
• Publication Date: 2016-07
• Subjects: Two-phase anaerobic digestion -- Fruit and vegetable waste -- Lactate -- Low pH acidification -- Upflow anaerobic sludge bed reactor; Biomass -- Periodicals; Biomass energy -- Periodicals; Bioremediation -- Periodicals; Agricultural wastes -- Periodicals; Factory and trade waste -- Periodicals; Organic wastes -- Periodicals; Bioénergie -- Périodiques; Déchets agricoles -- Périodiques; Déchets industriels -- Périodiques; Déchets organiques -- Périodiques; Déchets (Combustible) -- Périodiques; 662.88
• DOI: 10.1016/j.biortech.2016.03.050
• Languages: English
• ISSNs: 0960-8524

Abstract

Highlights: A novel method of two-phase anaerobic digestion is proposed. Acid reactor was operated at pH 4.0 with lactate as dominant product. Effluent from acid reactor was efficiently degraded in UASB. Lactobacillus was the predominant microorganism in the acid reactor. Hydrogenotrophic methanogens enriched in methane reactor after acclimation. Abstract: A novel method of two-phase anaerobic digestion where the acid reactor is operated at low pH 4.0 was proposed and investigated. A completely stirred tank acid reactor and an up-flow anaerobic sludge bed methane reactor were operated to examine the possibility of efficient degradation of lactate and to identify their optimal operating conditions. Lactate with an average concentration of 14.8 g/L was the dominant fermentative product and Lactobacillus was the predominant microorganism in the acid reactor. The effluent from the acid reactor was efficiently degraded in the methane reactor and the average methane yield was 261.4 ml/g COD removed. Organisms of Methanosaeta were the predominant methanogen in granular sludge of methane reactor, however, after acclimation hydrogenotrophic methanogens enriched, which benefited for the conversion of lactate to acetate. The two-phase AD system exhibited a low hydraulic retention time of 3.56 days and high methane yield of 348.5 ml/g VS removed.