Abstract

Various pretreatment methods have been combined and employed for maximizing the solubilization of waste-activated sludge (WAS). However, the question “by changing the series of applied combined pretreatments (CPs), can the solubilization efficiency of WAS be affected?” has never been addressed. In this study, firstly, thermal (T), alkaline (A), and ultrasonic (U) pretreatments were individually applied at broad strengths (T = 80–120 °C for 30 min, A = pH 9–12, and U = 5–60 min at 300 W). Then, pretreatment conditions that caused similar solubilization (13.0%) (120 °C, pH 11, and 30 min for T, A, and U, respectively), were adopted for CP with reverse sequences of T&A, U&A, and T&U. A similar disintegration degree was observed in U→A and A→U, while a meaningful difference was found in T&A and T&U: T→A (28.3%), A→T (42.9%), T→U (22.9%), and U→T (27.1%). The difference in pretreatment series also affected the characteristics of soluble matters, which was analyzed by excitation emission matrix and molecular weight distribution. Due to these differences, the highest methane yield of 68.8% (based on (chemical oxygen demand) CODinput) was achieved at A→T, compared to T→A (62.3%). Our results suggested a simple strategy for increasing solubilization, at the same expense of energy, which might be beneficial in the following treatment process, such as dewatering and transportation.

Highlights

  • By the development and increase in the number of wastewater treatment plants, the amount of sludge that is discharged is increasing [1]

  • Altering the sequence of the combined pretreatments (CPs) set affected the achieved disintegration degree (DD); a variation in solubilization impact was noticed among various CP sets

  • Altering the sequence in cases of T&A and T&U could affect the solubilization of waste-activated sludge (WAS), while altering the sequence in case of U&A did not lead to the significant change in the acquired solubilization

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Summary

Introduction

By the development and increase in the number of wastewater treatment plants, the amount of sludge that is discharged is increasing [1]. Because of the non-biodegradable fraction contained in sludge and its high viscous characteristics, the management of the sludge costs more than half of the costs dedicated for wastewater treatment plants’ operation [2,3]. There are largely two types of sludge: primary sludge and waste-activated sludge (WAS), which are made of organic matters, recalcitrant matters, alive microbes, and water. Primary sludge contains mainly biodegradable matters, it can be treated [4,5]. WAS treatment is mandatory, it is still a problematic issue, because of the recalcitrant content found in Energies 2020, 13, 4165; doi:10.3390/en13164165 www.mdpi.com/journal/energies

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