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Enhancement of biomethane production from the anaerobic co-digestion of sewage sludge and macroalgae by continuous and intermittent addition of glycerol

机译:通过连续和间歇添加甘油,厌氧消化下水道污泥和大型藻类的共消化,可提高生物甲烷的生产量

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摘要

Anaerobic digestion(AD) is a multifunctional bioprocess that allows nutrient recycling and reduction, production of biogas, and a sustainable bioenergy carrier. AD of macroalgae presents a promising source of bioenergy in the future. Macroalgae have high concentration of carbohydrates, making it suitable for biogas production, not competing with food crops for arable land and irrigation water.This work aimed to enhance the methane (CH4) production from the anaerobic co- digestion of a mixture of sewage sludge (SS from a wastewater treatment plant) and Ulva sp. (Ulv macroalgae), with continuous and intermittent addition of crude glycerol (cGly from vegetable oils), in a semi-continuous system.Three 5 L stirred tank reactors (R1, R2 and R3) were fed with SS and Ulv (85/15 in total solids). The reactors were operated at 37 °C, with a 4 L working volume and inoculated with anaerobic granular sludge from a brewery industry. Until day 179, the reactors were fed only with SS, while the hydraulic retention time (HRT) has been continuously decreasing from 40 d to 20 d. After reaching stabilization at HRT of 20 d, Ulv and cGly were added to feed (until day 241). R1 was the control, without cGly. In R2, cGly was continuously supplemented, 2 % (w) of the mixture of SS and Ulv. In R3, pulses of cGly were applied once a week, with same amount introduced in R2 since the last pulse.The AD of SS with an organic loading rate (g of COD of substrate per L of reactor and time) of 3.33 g L-1 d-1 achieved a CH4 production (MP, expressed in L of CH4 produced per kg of chemical oxygen demand (COD) of substrate fed L kg-1)) of 166 L kg-1 with 39 % of volatile solid (VS) reduction. The addition of Ulv (R1) decreased the MP in 20%. The continuous introduction of cGly (R2) improved significantly the MP, reaching 204 L kg-1 (51 % of VS reduction). Noteworthy, the intermittent addition of cGly (R3) showed the best results in terms of MP, 251 L kg-1 achieving 56 % of VS reduction.
机译:厌氧消化(AD)是一个多功能的生物过程,可进行营养物的循环利用和减少,沼气的产生以及可持续的生物能源载体。大型藻类的AD代表了未来有希望的生物能源来源。大型藻类中碳水化合物的浓度高,使其适合用于沼气生产,不与粮食作物争夺可耕地和灌溉用水。这项工作旨在提高厌氧性共消化污水污泥混合物产生的甲烷(CH4)(来自污水处理厂的SS)和Ulva sp。 (Ulv大型藻类),在半连续系统中连续和间歇地添加粗甘油(来自植物油的cGly)。三个5 L搅拌釜反应器(R1,R2和R3)分别加入SS和Ulv(85/15)总固体)。反应器在37°C下运行,工作容积为4 L,并接种了啤酒厂的厌氧颗粒污泥。直到第179天,反应器仅加入SS,而水力停留时间(HRT)从40 d连续减少到20 d。在HRT 20天达到稳定后,将Ulv和cGly添加到饲料中(直到第241天)。 R1是对照,没有cGly。在R2中,连续补充cGly 2%(w)的SS和Ulv的混合物。在R3中,每周一次施加cGly脉冲,自上次脉冲以来在R2中引入的脉冲量相同.SS的AD的有机负载率(每升反应器和时间的底物COD克数和时间)为3.33 g L- 1 d-1实现了166 L kg-1的CH4产量(MP,以每千克进料L kg-1的底物的化学需氧量(COD)产生的CH4的L表示))和39%的挥发性固体(VS)减少。添加Ulv(R1)可使MP降低20%。连续引入cGly(R2)显着改善了MP,达到204 L kg-1(VS降低51%)。值得注意的是,间歇性添加cGly(R3)在MP方面显示出最好的结果,251 L kg-1实现了VS降低56%。

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