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黑水和厨余垃圾的源头分离及厌氧共消化用于沼气生产和营养物回收。

Source separation and anaerobic co-digestion of blackwater and food waste for biogas production and nutrient recovery.

机构信息

Department of Bioproducts and Biosystems, School of Chemical Engineering, Aalto University, 02150 Espoo, Finland; Faculty of Engineering and Natural Sciences, Materials Science and Environmental Engineering, Tampere University, Tampere, Finland E-mail:

Faculty of Engineering and Natural Sciences, Materials Science and Environmental Engineering, Tampere University, Tampere, Finland.

出版信息

Water Sci Technol. 2024 Aug;90(3):1082-1098. doi: 10.2166/wst.2024.251. Epub 2024 Jul 22.

Abstract

Anaerobic co-digestion of source-separated blackwater (BW) and food and kitchen waste (FW) offers decentralized circular economy solutions by enabling local production of biogas and nutrient-rich byproducts. In this study, a 2 m pilot-scale continuously stirred tank reactor (CSTR) operated under mesophilic conditions was utilized for co-digestion of BW and FW. The process obtained a CH yield of 0.7 ± 0.2 m/kg influent-volatile solid (VS), reaching a maximum yield of 1.1 ± 0.1 m/kg influent-VS, with an average organic loading rate of 0.6 ± 0.1 kg-VS/m/d and HRT of 25 days. The CH production rate averaged 0.4 ± 0.1 m/m/d, peaking at 0.6 ± 0.1 m/m/d. Treatment of digestate through flocculation followed by sedimentation recovered over 90% of ammonium nitrogen and potassium, and 80-85% of total phosphorus in the liquid fraction. This nutrient-rich liquid was used to cultivate , achieving a biomass concentration of 1.2 ± 0.1 g/L and 85 ± 3% and 78 ± 5% ammonium nitrogen and phosphorus removal efficiency, respectively. These findings not only highlight the feasibility of anaerobic co-digestion of source-separated BW and FW in local biogas production but also demonstrate the potential of microalgae cultivation as a sustainable approach to converting digestate into nutrient-rich algae biomass.

摘要

以黑水 (BW) 和食物及厨房废物 (FW) 为原料的厌氧共消化为沼气和营养丰富的副产物提供了分散式循环经济解决方案。本研究采用 2m3 中温连续搅拌槽式反应器 (CSTR) 进行共消化。该工艺的 CH4 产率为 0.7±0.2m3/kg 进料-挥发性固体 (VS),最大产率达到 1.1±0.1m3/kg 进料-VS,平均有机负荷率为 0.6±0.1kg-VS/m3/d,水力停留时间为 25 天。CH4 产率平均为 0.4±0.1m3/m3/d,最高达 0.6±0.1m3/m3/d。通过絮凝和沉淀处理消化液,可回收超过 90%的铵态氮和钾,以及 80-85%的液体部分总磷。这种富营养化的液体被用来培养 ,生物量浓度达到 1.2±0.1g/L,铵态氮和磷的去除效率分别达到 85±3%和 78±5%。这些发现不仅突出了在当地沼气生产中进行黑水 (BW) 和食物及厨房废物 (FW) 分离源厌氧共消化的可行性,还展示了利用微藻培养作为一种可持续的方法将消化液转化为营养丰富的藻类生物量的潜力。

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