Abstract

Neutralization with liquid digestate and CO2 was compared herein to adjust the pH of lime-treated corn stover. The effects on the thermophilic (55 °C) anaerobic digestion were also analyzed. Liquid digestate neutralization (LDN) caused a decrease in pH from 10.5 to 7.5 in 60 h and accumulation of acetic/isobutyric acids. The CO2 neutralization (CN) under solid-state conditions reduced the pH from 10.5 to 8.5 in 30 min, which is faster than that of LDN and did not affect the subsequent anaerobic digestion. Biomethane production rate indicates that LDN contributed to the performance of anaerobic digestion, but this was not sufficient to compensate for the loss of total biomethane yield, resulting in a negative net profit (i.e., revenue from increased energy production minus reagent cost). For CN under solid-state conditions, the biomethane production was highest in both liquid- and solid-state anaerobic digestion, and also obtained a net profit of 98.74–100.89 RMB/tonne dry biomass. Therefore, the solid-state condition CN is a more efficient and economic method for adjusting initial pH of lime-treated corn stover.

Highlights

  • IntroductionAnaerobic digestion (AD) is an environment-friendly and sustainable technology for the treatment of agricultural residues for recovering energy in the form of biogas and organic fertilizer raw materials in the form of digestates [1,2]

  • Anaerobic digestion (AD) can be categorized according to the total solids (TS) content as liquid AD (L-AD) and solid-state AD (SS-AD) [3], and it can be grouped into mesophilic AD (30–40 ◦ C) and thermophilic AD (50–60 ◦ C), according to the operating temperature [4,5]

  • Two novel neutralization methods for lime-treated corn stover (CS) were developed for biomethane production: (1) Liquid digestate (LD)-neutralization and (2) CO2 -neutralization

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Summary

Introduction

Anaerobic digestion (AD) is an environment-friendly and sustainable technology for the treatment of agricultural residues for recovering energy in the form of biogas and organic fertilizer raw materials in the form of digestates [1,2]. AD can be categorized according to the total solids (TS) content as liquid AD (L-AD) and solid-state AD (SS-AD) [3], and it can be grouped into mesophilic AD (30–40 ◦ C) and thermophilic AD (50–60 ◦ C), according to the operating temperature [4,5]. As less moisture increases equipment efficiency and reduces heating demand [6], while higher fermentation temperatures accelerate biogas production and reduce retention time [4], a growing corpus of studies has been focused on thermophilic SS-AD [7,8,9]

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