Efficiency of integrated electrooxidation and anaerobic digestion of waste activated sludge

被引:15
|
作者
Barrios, J. A. [1 ]
Cano, A. [1 ]
Rivera, F. F. [2 ]
Cisneros, M. E. [1 ]
Duran, U. [1 ]
机构
[1] Univ Nacl Autonoma Mexico, Inst Ingn, POB 70-186, Mexico City 04510, DF, Mexico
[2] CONACYT Ctr Invest & Desarrollo Tecno Electroquim, Parque Tecnol Queretaro S-N, Mexico City 76703, DF, Mexico
关键词
Anaerobic digestion; Waste activated sludge; Pre-treatment; Electrooxidation; Energy analysis; ELECTROCHEMICAL OXIDATION; SEWAGE-SLUDGE; TREATMENT TECHNOLOGIES; WATER; PRETREATMENT; DISINTEGRATION; SOLUBILIZATION; FEASIBILITY; DYE;
D O I
10.1186/s13068-021-01929-7
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Background: Most of the organic content of waste activated sludge (WAS) comprises microbial cells hard to degrade, which must be pre-treated for energy recovery by anaerobic digestion (AD). Electrooxidation pre-treatment (EOP) with boron-doped diamond (BDD) electrode have been considered a promising novel technology that increase hydrolysis rate, by the disintegrating cell walls from WAS. Although electrochemical oxidation could efficiently solubilize organic substances of macromolecules, limited reports are available on EOP of WAS for improving AD. In this endeavour, the mathematical optimization study and the energy analysis of the effects of initial total solids concentrations [TS] of WAS and current density (CD) during EOP on the methane production and removal of chemical oxygen demand (COD) and volatile solids (VS) were investigated. Because limited reports are available on EOP of WAS for improving biogas production, it is not well understood; however, it has started to attract interest of scientists and engineers. Results: In the present work, the energy recovery as biogas and WAS conversion were comprehensively affected by CD and [TS], in an integrated EOP and AD system. When working with WAS at 3% of [TS] pre-treated at current density of 24.1 mA/cm(2), the highest COD and VS removal were achieved, making it possible to obtain the maximum methane (CH4) production of 305 N-L/kg VS and a positive energy balance of 1.67 kWh/kg VS. Therefore, the current densities used in BDD electrode are adequate to produce the strong oxidant (hydroxyl radical, (OH)-O-center dot) on the electrode surface, allow the oxidation of organic compounds that favours the solubilization of particulate matter and VS from WAS. Conclusions: The improvement of VS removal and COD solubilization were due to the effects of pre-treatments, which help to break down the microbial cells for faster subsequent degradation; this allows a decomposition reaction that leads to biodegrade more compounds during AD. The balance was positive, suggesting that even without any optimization the energy used as electricity could be recovered from the increased methane production. It is worth noting that this kind of analysis have not been sufficiently studied so far. It is therefore important to understand how operational parameters can influence the pre-treatment and AD performances. The current study highlights that the mathematical optimization and energy analysis can make the whole process more convenient and feasible.
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页数:9
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