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采用液态和固态耦合厌氧消化法从棕榈油厂废水和空果串中生产沼气。

Biogas production from palm oil mill effluent and empty fruit bunches by coupled liquid and solid-state anaerobic digestion.

机构信息

Biotechnology Program, Faculty of Science, Thaksin University, Phatthalung 93210, Thailand.

Chemistry Division, Department of Science, Faculty of Science and Technology, Prince of Songkla University, Pattani 94000, Thailand.

出版信息

Bioresour Technol. 2020 Jan;296:122304. doi: 10.1016/j.biortech.2019.122304. Epub 2019 Oct 21.

Abstract

Biogas production of palm oil mill effluent (POME) and empty fruit bunches (EFB) was performed by coupled liquid (L-AD) and solid-state (SS-AD) anaerobic digestion processes. POME was fed to L-AD digester, while mixed of effluent from L-AD and EFB was fed to SS-AD digester. The maximum overall methane production of 60.9 m-CH·ton waste was obtained at an optimal hydraulic retention time of 30 days and an organic loading rate of 1.66 gVS·L-reactor·d for L-AD and 6.03 gVS·L-reactor·d for SS-AD with L-AD effluent recycling rate of 16.7 mL·L-reactor·d. The bacterial community in the L-AD reactor was different from the SS-AD reactor, while the archaeal community was similar in both reactors. Synergistaceae, Caldicoprobacteraceae and Lachnospiraceae were increased in the SS-AD reactor. Coupling L-AD and SS-AD is able to increase energy production by 29% and 71% compared to the L-AD and SS-AD alone, respectively, with no outsource SS-AD inoculum required.

摘要

采用液态(L-AD)和固态(SS-AD)厌氧消化工艺对棕榈油废水(POME)和空果串(EFB)进行沼气生产。将 POME 进料至 L-AD 消化器,而将来自 L-AD 的流出物与 EFB 的混合物进料至 SS-AD 消化器。在最佳水力停留时间为 30 天和有机负荷率为 1.66 gVS·L-reactor·d 时,L-AD 的整体最大甲烷产量为 60.9 m-CH·吨废物,而 SS-AD 的整体最大甲烷产量为 6.03 gVS·L-reactor·d,L-AD 流出物再循环率为 16.7 mL·L-reactor·d。L-AD 反应器中的细菌群落与 SS-AD 反应器中的细菌群落不同,而古菌群落在两个反应器中相似。协同菌科、Caldicoprobacteraceae 和 Lachnospiraceae 在 SS-AD 反应器中增加。与单独的 L-AD 和 SS-AD 相比,耦合 L-AD 和 SS-AD 分别能够将能源产量提高 29%和 71%,而无需外部供应 SS-AD 接种物。

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