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Optimization of hydrothermal pretreatment conditions for mesophilic and thermophilic anaerobic digestion of high-solid sludge.
Wu, Li-Jie; Li, Xiao-Xiao; Liu, Yu-Xiang; Yang, Fan; Zhou, Quan; Ren, Rui-Peng; Lyu, Yong-Kang.
Afiliação
  • Wu LJ; Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Taiyuan University of Technology, Taiyuan 030024, China. Electronic address: wulijie@tyut.edu.cn.
  • Li XX; College of Environmental Science and Engineering, Taiyuan University of Technology, Taiyuan 030024, China.
  • Liu YX; College of Environmental Science and Engineering, Taiyuan University of Technology, Taiyuan 030024, China.
  • Yang F; Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Taiyuan University of Technology, Taiyuan 030024, China.
  • Zhou Q; Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Taiyuan University of Technology, Taiyuan 030024, China.
  • Ren RP; Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Taiyuan University of Technology, Taiyuan 030024, China.
  • Lyu YK; Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Taiyuan University of Technology, Taiyuan 030024, China.
Bioresour Technol ; 321: 124454, 2021 Feb.
Article em En | MEDLINE | ID: mdl-33285502
ABSTRACT
Hydrothermal pretreatment (HTP) conditions were optimized for continuous mesophilic (MAD) and thermophilic (TAD) anaerobic digestion of high-solid sludge (10-11% total solids). COD solubilization increased with prolonged HTP durations, and became not significant after 210 min. According to the methane production rate and energy consumption, the optimal HTP temperature was determined at 160 °C. Regarding continuous operation without HTP, TAD achieved higher methane yield and volatile solids (VS) reduction, at 0.12 L/g VSadded and 23.9%, respectively. After HTP, methane yield and VS reduction in MAD and TAD were increased by 400% and 191% (MAD), 67% and 72% (TAD), respectively. TAD was limited due to the inhibition from about 2800 mg/L of NH4+-N concentration. The methanogenic activity of MAD was enhanced, whereas TAD displayed a reduced value owing to ammonia inhibition. Ultimately, MAD with HTP and TAD without HTP achieved the higher energy balance, 5.25 and 3.27 kJ/g VS, respectively.
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Texto completo: 1 Base de dados: MEDLINE Assunto principal: Esgotos / Metano Idioma: En Ano de publicação: 2021 Tipo de documento: Article

Texto completo: 1 Base de dados: MEDLINE Assunto principal: Esgotos / Metano Idioma: En Ano de publicação: 2021 Tipo de documento: Article