Kinetics of Anaerobic Digestion of Palm Oil Mill Effluent (POME) in Double-Stage Batch Bioreactor with Recirculation and Fluidization of Microbial Immobilization Media

Quality in Research: International Symposium on Materials, Metallurgy, and Chemical Engineering

材料科学;冶金学;化学工业

Ramadhani, L.I.^1 ; Damayanti, S.I.^1 ; Sudibyo, H.^1,2 ; Budhijanto, W.^1,2

Chemical Engineering Department, Universitas Gadjah Mada, Yogyakarta

55281, Indonesia^1

Center for Energy Studies, Universitas Gadjah Mada, Yogyakarta

55281, Indonesia^2

关键词: Anaerobic fluidized bed reactors;    Batch bioreactors;    Chemical oxygen demand removals;    Conventional methods;    Microbial immobilization;    Optimum fluidization;    Palm oil mill effluents;    Renewable energy source;   

Others  :  https://iopscience.iop.org/article/10.1088/1757-899X/316/1/012071/pdf
DOI  :  10.1088/1757-899X/316/1/012071

学科分类：材料科学（综合）

来源: IOP

【 摘 要 】

Palm Oil Mill Effluent (POME) becomes big problem for palm oil industries, especially for Crude Palm Oil (CPO) industry since it produces 3 tons of POME for every ton of CPO production.The high amount of organic loading in POME makes it potential as a substrate in anaerobic digestion to generate biogas as renewable energy source. The most common but conventional method by using open lagoon is still preferred for most CPO industry in Indonesia to treat POME because of its simplicity and easiness. However, this method creates new major problem for the water bodies since it has no significant chemical oxygen demand (COD) removal and needs wide area. Besides, greenhouse gas (CH4) is also released during the process. An innovation was made in this study by designing vertical column process equipment to run an anaerobic digestion of POME. The vertical column was functioned as anaerobic fluidized bed reactor (AFBR). To enhance the digestion rate in AFBR, natural zeolite was used as the immobilization media and the inoculum was taken from digested biodiesel waste. This research aimed to determine the kinetic constants of double-stage anaerobic POME digestion for COD removal and biogas production. To get close to the real condition, the POME used in this experiment had 8,000 mg/L of sCOD (the real sCOD was ±16,000 mg/L). The experiment was conducted under room temperature with up-flow velocity between 1.75 and 2.3 cm/s for optimum fluidization of immobilization media.