Innovative system to maximize methane production from fruit and vegetable waste

被引:0
|
作者
Camila Aparecida de Menezes [1 ]
Daniel Rodrigues dos Santos [2 ]
Willame de Araújo Cavalcante [3 ]
Priscilla de Souza Almeida [1 ]
Thobias Pereira Silva [2 ]
Francisco das Chagas Gomes da Silva Júnior [4 ]
Tito Augusto Gehring [5 ]
Marcelo Zaiat [4 ]
André Bezerra dos Santos [2 ]
Renato Carrhá Leitão [1 ]
机构
[1] Embrapa Tropical Agroindustry,Department of Hydraulic and Environmental Engineering
[2] Federal University of Ceará,São Carlos School of Engineering
[3] Federal Institute of Education,Institute of Urban Water Management and Environmental Engineering, Department of Civil and Environmental Engineering
[4] Science,undefined
[5] and Technology of Ceará,undefined
[6] University of São Paulo,undefined
[7] Ruhr-Universität Bochum,undefined
关键词
Food waste; Up-flow anaerobic sludge blanket reactor; Dry anaerobic digestion; Dranco system; Anaerobic Digestion Model 1; Anaerobic digestion;
D O I
10.1007/s11356-024-35328-w
中图分类号
学科分类号
摘要
Anaerobic digestion of fruit and vegetable waste (FVW) offers an environmentally friendly alternative for waste disposal, converting it into methane for energy recovery. Typically, FVW digestion is conducted in a continuously stirred tank reactor (CSTR) due to its ease of use and stability with solid concentrations between 5 and 10%. However, CSTRs are limited to organic loading rates (OLRs) of about 3 kg COD/m3.day, resulting in large reactor volumes, low methane productivity, and costly wet digestate handling. This work introduces a novel method for methane production from FVW using a high-rate reactor system. The proposed approach involves grinding, centrifuging, and/or pressing the FVW to separate it into liquid and solid phases. The liquid phase is then digested in an up-flow anaerobic sludge blanket (UASB) reactor, while the solid phase undergoes digestion in a dry methanization reactor. A model incorporating all biological reactors was implemented in the Anaerobic Digestion Model 1 (ADM1) to provide a theoretical basis for the experimental development of this system. The current simulation scenarios offer initial references for operating the experimental system, which will, in turn, generate data for further model refinement. For instance, constrained liquid–gas mass transfer was considered for dry fermentation, with additional potential biochemical kinetic limitations to be incorporated following on experimental evidence. The success of this system could enable energy recovery in 72 Central Wholesale Markets across Brazil, offering a critical tool for planning, operating, and optimizing such systems.
引用
收藏
页码:62825 / 62839
页数:14
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