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固态厌氧消化小麦秸秆:S/I 比和中试真菌预处理的影响。

Solid-state anaerobic digestion of wheat straw: Impact of S/I ratio and pilot-scale fungal pretreatment.

机构信息

LBE, Univ. Montpellier, INRA, 102 Avenue des Etangs, F-11100 Narbonne, France.

LBE, Univ. Montpellier, INRA, 102 Avenue des Etangs, F-11100 Narbonne, France.

出版信息

Waste Manag. 2019 Feb 15;85:464-476. doi: 10.1016/j.wasman.2019.01.006. Epub 2019 Jan 16.

DOI:10.1016/j.wasman.2019.01.006
PMID:30803602
Abstract

Solid State Anaerobic Digestion (SSAD) of fungal pretreated wheat straw was evaluated in a leach bed reactor. During a first experiment, the effect of Substrate/Inoculum (S/I) ratios on the start-up phase was investigated. High S/I increased methane productivity but also raised the risk of reactor failure due to Volatile Fatty Acid (VFA) accumulation. With S/I ratios between 1.2 and 3.6 (Volatile Solid (VS) basis), the SSAD start-up using wheat straw was successful. Moreover, reactors were able to recover from acidification when the Total VFA/alkalinity ratio was lower than 2 gHAc_eq/gCaCO, with VFA concentrations lower than 10 g/L and a pH close to 5.5. The conventional threshold of 0.6 gHAc_eq/gCaCO for stable wet AD is therefore not adapted to SSAD. During a second experiment, after the wheat straw was submitted to a fungal pretreatment in a non-sterile pilot-scale reactor, it was digested with an S/I ratio of 2.8-2.9. Under batch SSAD conditions, the biodegradability of pretreated wheat straw was slightly improved in comparison to the control (254 versus 215 NmL/g VS, respectively). Considering mass losses occurring during the pretreatment step, suboptimal pretreatment conditions caused a slightly lower methane production (161 versus 171 NmL/gTS after 60-days anaerobic digestion). Nevertheless, pretreatment improved the start-up phase with lower acidification relative to controls. It would be particularly beneficial to improve the methane production in reactors with short reaction times.

摘要

固态厌氧消化(SSAD)真菌预处理小麦秸秆在渗滤床反应器中进行了评估。在第一个实验中,研究了底物/接种物(S/I)比对启动阶段的影响。高 S/I 提高了甲烷产率,但也增加了由于挥发性脂肪酸(VFA)积累而导致反应器故障的风险。当 S/I 比在 1.2 到 3.6(挥发性固体(VS)基础)之间时,使用小麦秸秆的 SSAD 启动是成功的。此外,当总 VFA/碱度比低于 2 gHAc_eq/gCaCO 时,反应器能够从酸化中恢复过来,此时 VFA 浓度低于 10 g/L,pH 值接近 5.5。因此,传统的湿式 AD 稳定的 0.6 gHAc_eq/gCaCO 阈值不适应 SSAD。在第二个实验中,小麦秸秆在非无菌中试规模反应器中进行真菌预处理后,用 S/I 比为 2.8-2.9 进行消化。在分批 SSAD 条件下,与对照相比,预处理小麦秸秆的生物降解性略有提高(分别为 254 与 215 NmL/g VS)。考虑到预处理步骤中发生的质量损失,次优预处理条件导致甲烷产量略低(60 天厌氧消化后分别为 161 与 171 NmL/gTS)。然而,预处理相对于对照改善了启动阶段,酸化程度较低。对于具有短反应时间的反应器,改善甲烷产量将特别有益。

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