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A Kinetic Model for Anaerobic Digestion and Biogas Production of Plant Biomass under High Salinity

Author

Listed:
  • Jing Wang

    (School of Municipal and Environmental Engineering, Shandong Jianzhu University, Jinan 250101, China)

  • Bing Liu

    (Resources and Environment Innovation Research Institute, Shandong Jianzhu University, Jinan 250101, China)

  • Meng Sun

    (Faculty of Environmental Engineering, The University of Kitakyushu, 1-1, Hibikino, Wakamatsu, Kitakyushu 808-0135, Japan)

  • Feiyong Chen

    (Resources and Environment Innovation Research Institute, Shandong Jianzhu University, Jinan 250101, China)

  • Mitsuharu Terashima

    (Faculty of Environmental Engineering, The University of Kitakyushu, 1-1, Hibikino, Wakamatsu, Kitakyushu 808-0135, Japan)

  • Hidenari Yasui

    (Faculty of Environmental Engineering, The University of Kitakyushu, 1-1, Hibikino, Wakamatsu, Kitakyushu 808-0135, Japan)

Abstract

The aim of this study is to evaluate the anaerobic digestion and biogas production of plant biomass under high salinity by adopting a theoretical and technical approach for saline plant-biomass treatment. Two completely mixed lab-scale mesophilic reactors were operated for 480 days. In one of them, NaCl was added and the sodium ion concentration was maintained at 35.8 g-Na + ·L −1 , and the organic loading rate was 0.58-COD·L −1 ·d −1 –1.5 g-COD·L −1 ·d −1 ; the other added Na 2 SO 4 –NaHCO 3 and kept the sodium ion concentration at 27.6 g-Na + ·L −1 and the organic loading rate at 0.2 g-COD·L −1 ·d −1 –0.8 g-COD·L − 1 ·d −1 . The conversion efficiencies of the two systems (COD to methane) were 66% and 54%, respectively. Based on the sulfate-reduction reaction and the existing anaerobic digestion model, a kinetic model comprising 12 types of soluble substrates and 16 types of anaerobic microorganisms was developed. The model was used to simulate the process performance of a continuous anaerobic bioreactor with a mixed liquor suspended solids (MLSS) concentration of 10 g·L −1 –40 g·L −1 . The results showed that the NaCl system could receive the influent up to a loading rate of 0.16 kg-COD/kg-MLSS·d −1 without significant degradation of the methane conversion at 66%, while the Na 2 SO 4 –NaHCO 3 system could receive more than 2 kg-COD·kg −1 -MLSS·d −1 , where 54% of the fed chemical oxygen demand (COD) was converted into methane and another 12% was observed to be sulfide.

Suggested Citation

  • Jing Wang & Bing Liu & Meng Sun & Feiyong Chen & Mitsuharu Terashima & Hidenari Yasui, 2022. "A Kinetic Model for Anaerobic Digestion and Biogas Production of Plant Biomass under High Salinity," IJERPH, MDPI, vol. 19(11), pages 1-20, June.
    • Handle: RePEc:gam:jijerp:v:19:y:2022:i:11:p:6943-:d:832551
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    References listed on IDEAS

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