间歇反应器中以牛粪和牛瘤胃液为接种物的咖啡浆废渣产沼气性能研究

T. Widjaja, Nurkhamidah, A. Altway, T. Iswanto, E. Grady
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引用次数: 0

摘要

从咖啡浆废料中生产沼气是印度尼西亚提供替代能源的潜在尝试之一。作为印度尼西亚的主要商品,咖啡在加工过程中产生的残余废物,如纸浆废物(包括外果皮、中果皮和内果皮)。废水中含有咖啡因、单宁、游离酚等有毒物质,可抑制沼气的产生。因此,本研究采用果子狸粪便进行生物预处理。研究了以牛粪和瘤胃液-牛粪混合液为接种剂,对咖啡浆(经过预处理和未经过预处理)产气的性能和动力学。在一个工作容积为3.6升的反应器中,在37℃的中温条件下厌氧生产了40天的沼气。测定的参数包括抑制剂组分、TS、VS、COD、产气量、动力学参数等。本研究表明,果子狸粪预处理可以减少咖啡浆废弃物中抑制剂的含量,从而产生浓度高于未预处理的甲烷。添加预处理咖啡浆、牛粪和瘤胃液的沼气池产气效果最佳。动力学参数为k (0.0446 d -1)、Y (0.056 g细胞/g底物)、μ m (0.0688 d -1)、k s (25.2359 g/L)和Y m(43.299)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Performance of Biogas Production from Coffee Pulp Waste with Cow Dung and Cattle Rumen Fluid as Inoculum in a Batch Reactor
Production of biogas from coffee pulp waste is one of the potential attempts to provide alternative energy in Indonesia. As a leading commodity in Indonesia, the coffee produced the residual waste from its processing such as the pulp waste (include the exocarp, mesocarp, and endocarp). The waste contains the toxic agent such as caffeine, tannin, and free phenols which can inhibit the biogas production. Therefore, in this study, the biological pretreatment using civet feces ( Paradoxurus hermaphroditus ) was performed. The performance and kinetic of biogas formation from the coffee pulp (with and without pretreatment) using cow dung and a mixture of rumen fluid and cow dung as inoculum have been investigated. Biogas production was done anaerobically for 40 days at mesophilic temperature (37  o C) in a reactor with a working volume of 3.6 liters. Measured parameters included the inhibitor components, TS, VS, COD, production of biogas, and kinetic parameters. This study reveals that the pretreatment using civet feces could reduce the inhibitor compounds in the coffee pulp waste leading to produce methane in higher concentration than those without pretreatment. The digester containing pretreated coffee pulp with cow dung and rumen fluid addition showed the best performance of biogas formation. Kinetic parameters which were obtained from the fourth digester were k (0.0446 day -1 ), Y (0.056 g cells/g substrate), μ m (0.0688 day -1 ), K s (25.2359 g/L), and y m (43.299).
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