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(Reference retrieved automatically from Web of Science through information on FAPESP grant and its corresponding number as mentioned in the publication by the authors.)

Anaerobic Biodegradation of Biodiesel Industry Wastewater in Mesophilic and Thermophilic Fluidized Bed Reactors: Enhancing Treatment and Methane Recovery

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Author(s):
da Costa, Talles Barcelos [1] ; Simoes, Andreza Nataline [2] ; de Menezes, Camila Aparecida [2] ; Silva, Edson Luiz [1]
Total Authors: 4
Affiliation:
[1] Univ Fed Sao Carlos, Dept Chem Engn, Rod Washington Luis, Km 235, BR-13565905 Sao Carlos, SP - Brazil
[2] Univ Sao Paulo, Sch Engn Sao Carlos, Dept Hydraul & Sanitat, Av Joao Dagnone 1100 Jd Santa Angelina, BR-13563120 Sao Carlos, SP - Brazil
Total Affiliations: 2
Document type: Journal article
Source: Applied Biochemistry and Biotechnology; v. 193, n. 10, p. 3336-3350, OCT 2021.
Web of Science Citations: 0
Abstract

In the past few years, the extraction of value-added compounds from the anaerobic digestion of glycerol has been an option to add value to this waste because biodiesel production is increasing worldwide. The evolution of research on glycerol valorization by anaerobic digestion has reached the use of high-rate reactors. However, no study has evaluated glycerol digestion in an anaerobic fluidized bed reactor (AFBR), a configuration with potential advantages in methane production. Still, the best operating temperature for high-rate glycerol digestion remains unclear. To clarify these gaps, the present study aimed to compare glycerol digestion in mesophilic AFBR (30 degrees C) and thermophilic AFBR (55 degrees C). In both reactors, glycerol concentration was increased from 1.0 to 7.0 g L-1 at a fixed hydraulic retention time of 24 h, resulting in an increase at the organic loading rate from 1.2 to 7.6 kg COD m(-3) day(-1). Thermophilic digestion of glycerol achieved superior removals of organic matter (67.7-94.2%) and methane yield (330.8 mL CH4 g(-1) COD) than the mesophilic digestion (48.6-93.0% and 266.6 mL CH4 g(-1) COD). Additionally, the application of the kinetic model of substrate utilization (modified Stover-Kincannon model) indicated a higher substrate utilization coefficient in the thermophilic AFBR (23.09 g L-1 day(-1)) than the mesophilic AFBR (7.14 g L-1 day(-1)). Therefore, the application of glycerol concentrations higher than 7.0 g L-1 in thermophilic AFBR should be further investigated. Also, given only operational results, the application of the AFBR in the two-stage anaerobic digestion of glycerol is recommended. (AU)

FAPESP's process: 15/06246-7 - Biorefinery concept applied to biological wastewater treatment plants: environmental pollution control coupled with material and energy recovery
Grantee:Marcelo Zaiat
Support Opportunities: Research Projects - Thematic Grants