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

机译:双阶段批量生物反应器棕榈油磨流出物(PAME)的厌氧消解动力学与微生物固定介质的再循环和流化

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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.
机译:棕榈油厂流出物(Pome)成为棕榈油产业的大问题,特别是对于原油棕榈油(CPO)行业,因为它为每吨CPO生产产生了3吨歌曲。池中的有机装载量大量潜力厌氧消化中的底物,以产生沼气作为可再生能源。通过使用开放式泻湖最常见但传统的方法仍然是印度尼西亚大多数CPO行业的优先考虑汇集,因为其简单性和容易性。然而,这种方法为水体创造了新的主要问题,因为它没有显着的化学需氧量(COD)去除并需要广泛的区域。此外,温室气体(CH4)也在此过程中释放。本研究通过设计垂直柱工艺设备进行了创新,以运行Pome的厌氧消化。垂直柱用作厌氧流化床反应器(AFBR)。为了增强AFRB中的消化率,使用天然沸石作为固定介质,从消化的生物柴油废物中取出鞘内。该研究旨在确定用于COD去除和沼气生产的双级厌氧沼泽消化的动力学常数。为了接近真实条件,本实验中使用的底线具有8,000毫克/ L的SCOD(实际SCOD为±16,000 mg / L)。该实验在室温下进行,在1.75-2.3cm / s之间的上流速进行,以最佳流化固定化介质。

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