Your browser doesn't support javascript.
loading
Spiral-Pipe Gas Anaerobic Digester.
Li, Minghao; Zhao, Xingling; Wu, Kai; Liang, Chengyue; Liu, Jing; Yang, Hong; Wang, Changmei; Yang, Bin; Yin, Fang; Zhang, Wudi.
Afiliación
  • Li M; Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Zhao X; Yunnan Research Center of Biogas Technology and Engineering, School of Energy and Environment Science, Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Wu K; Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Liang C; Yunnan Research Center of Biogas Technology and Engineering, School of Energy and Environment Science, Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Liu J; Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Yang H; Yunnan Research Center of Biogas Technology and Engineering, School of Energy and Environment Science, Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Wang C; Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Yang B; Yunnan Research Center of Biogas Technology and Engineering, School of Energy and Environment Science, Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Yin F; Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
  • Zhang W; Yunnan Research Center of Biogas Technology and Engineering, School of Energy and Environment Science, Yunnan Normal University, 768 Jvxian Street, Kunming, Yunnan 650500, PR China.
ACS Omega ; 9(22): 23202-23208, 2024 Jun 04.
Article en En | MEDLINE | ID: mdl-38854509
ABSTRACT
The reduction of carbon dioxide to methane using hydrogen is an important process in biogas production. However, designing gas anaerobic digesters (GADs) based on this reaction presents several challenges. In this study, we developed an innovative spiral-pipe gas anaerobic digester (SGAD) to increase the displacement distance between the bubbles, thus prolonging the gas retention time and facilitating the reduction of CO2 to CH4 via H2. The process was successfully demonstrated by using a CO2/H2 ratio of 13 and a gas-feeding rate of 3.9 L Lr -1 d-1. During the experiment, more than 98% of the CO2 and 96% of the H2 were consumed, resulting in biogas containing ca. 86-96% CH4. Additionally, we applied our proposed evaluation methodology for assessing GAD performance to evaluate the performance of the SGAD. This methodology serves as a reference for evaluating and designing GAD systems. The innovative design of the SGAD and the corresponding evaluation methodology offer new insights into the design of reactors.

Texto completo: 1 Bases de datos: MEDLINE Idioma: En Revista: ACS Omega Año: 2024 Tipo del documento: Article

Texto completo: 1 Bases de datos: MEDLINE Idioma: En Revista: ACS Omega Año: 2024 Tipo del documento: Article