Department of Chemical Engineering, Federal University of São Carlos, Rod. Washington Luis, km 235, CEP, São Carlos, SP, 13565-905, Brazil.
Department of Hydraulics and Sanitation, School of Engineering of São Carlos, University of São Paulo, Av. João Dagnone, 1100 - Jd. Santa Angelina, CEP, São Carlos, SP, 13563-120, Brazil.
Appl Biochem Biotechnol. 2021 Oct;193(10):3336-3350. doi: 10.1007/s12010-021-03606-9. Epub 2021 Jun 29.
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 °C) and thermophilic AFBR (55 °C). In both reactors, glycerol concentration was increased from 1.0 to 7.0 g L 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 day. Thermophilic digestion of glycerol achieved superior removals of organic matter (67.7-94.2%) and methane yield (330.8 mL CH g COD) than the mesophilic digestion (48.6-93.0% and 266.6 mL CH g 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 day) than the mesophilic AFBR (7.14 g L day). Therefore, the application of glycerol concentrations higher than 7.0 g L 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.
在过去的几年中,从甘油的厌氧消化中提取增值化合物已成为增加这种废物附加值的一种选择,因为全球范围内生物柴油的产量正在增加。通过厌氧消化对甘油进行增值的研究已经发展到使用高速率反应器。然而,还没有研究评估过在厌氧流化床反应器(AFBR)中消化甘油,这种配置在甲烷生产方面具有潜在优势。然而,用于高速率甘油消化的最佳操作温度仍不清楚。为了澄清这些差距,本研究旨在比较中温 AFBR(30°C)和高温 AFBR(55°C)中甘油的消化情况。在这两个反应器中,甘油浓度从 1.0 增加到 7.0 g/L,水力停留时间保持在 24 h 不变,从而使有机负荷率从 1.2 增加到 7.6 kg COD/m·d。高温消化甘油对有机物的去除率(67.7-94.2%)和甲烷产率(330.8 mL CH/g COD)均优于中温消化(48.6-93.0%和 266.6 mL CH/g COD)。此外,底物利用动力学模型(修正的Stover-Kincannon 模型)的应用表明,高温 AFBR 中的底物利用系数(23.09 g/L·d)高于中温 AFBR(7.14 g/L·d)。因此,应进一步研究在高温 AFBR 中应用高于 7.0 g/L 的甘油浓度。此外,鉴于仅有的运行结果,建议将 AFBR 应用于甘油的两段式厌氧消化。