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厌氧序批式反应器共消化乳清和甘油,为小型和中型乳品企业提供解决方案:环境合规与甲烷生产。

Anaerobic Sequencing Batch Reactors Co-digesting Whey and Glycerin as a Possible Solution for Small and Mid-size Dairy Industries: Environmental Compliance and Methane Production.

机构信息

São Carlos School of Engineering, University of São Paulo (EESC/USP), Av. Trabalhador São Carlense 400, Sao Carlos, SP, 13566-590, Brazil.

Mauá School of Engineering, Mauá Institute of Technology (EEM/IMT), Praça Mauá 1, São Caetano do Sul, SP, 09580-900, Brazil.

出版信息

Appl Biochem Biotechnol. 2020 Nov;192(3):979-998. doi: 10.1007/s12010-020-03372-0. Epub 2020 Jul 2.

Abstract

A significant part of whey generated in Brazil is from small and mid-size dairy companies. Cheese whey has great potential for methane production through anaerobic biological processes but presents instabilities due to its high biodegradability. To study an alternative for the destination of this residue, the aim of this work was to investigate methane from the co-digestion of whey with glycerin and its environmental compliance at 55 °C in an anaerobic sequencing batch biofilm reactor. The best performance indicators were obtained with an influent composed of 88% cheese whey and 12% glycerin (by volume), fed-batch mode and organic loading rate of 19.3 kgCOD m day at 55 °C. This operational condition allowed us to achieve a methane productivity of 203 molCH m day, a methane yield close to theoretical value, and to remove 68% of all organic matter in the influent. A kinetic metabolic model was fitted to the experimental data, which indicated methanogenesis with preference for the acetoclastic route. Finally, the energy production (approximately 197 MWh month) from an industrial scale reactor and its volume (three reactors of 152 m) were assessed for a mid-size dairy industry, which could save up to US$ 22,000.00 per month in oil demand.

摘要

巴西生产的乳清蛋白中,相当一部分来自于中小型乳制品公司。奶酪乳清蛋白通过厌氧生物过程具有产生甲烷的巨大潜力,但由于其高生物降解性而存在不稳定性。为了研究这种残留物的替代用途,本工作旨在研究在 55°C 的厌氧序批式生物膜反应器中,乳清与甘油共消化产生甲烷的情况及其环境合规性。在 55°C 下,采用体积比为 88%奶酪乳清和 12%甘油的进料分批模式和 19.3 kgCOD m 天的有机负荷率,可获得最佳性能指标。在此操作条件下,可实现 203 molCH m 天的甲烷产率、接近理论值的甲烷产率以及去除进水有机物的 68%。对实验数据进行了代谢动力学模型拟合,结果表明产甲烷菌优先利用乙酸途径。最后,对中型乳制品厂的工业规模反应器的能量产量(约 197 MWh 月)及其体积(三个 152m 的反应器)进行了评估,每月可节省高达 22000 美元的石油需求。

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