Performance and kinetic analysis of biogas production from co‐digestion of landfill leachate with pineapple peel in batch experiments DOI

Souwalak Jaroenpoj,

Qi Yu,

James Ness

et al.

Biofuels Bioproducts and Biorefining, Journal Year: 2024, Volume and Issue: unknown

Published: Nov. 22, 2024

Abstract This study examines the co‐digestion of landfill leachate (LFL) with pineapple peel, focusing on biogas production. The was conducted a lab‐scale batch anaerobic digester using 30 L working volume completely mixed reactor at 35 °C to investigate monodigestion and peel their three different mixing ratios. results all experiments in were fitted first‐order kinetic models compare behavior batches through rate constants ( k ). As expected, digestion 25 achieved yield 38 kg −1 volatile solids (VS) consumed VS removal efficiency 30%, both markedly lower than those 3 per m tap water (513 80% efficiency). leachate, which had fixed L, 1, 2, −3 . showed that 2 highest 431 approximately 90% chemical oxygen demand (COD) stable conditions reactor. kinetics equation selected characterize able describe processes experiments. ) 0.25, 0.22, 0.18 day for

Language: Английский

Engineering application on the combination of simultaneous partial nitrification and denitrification and anammox for advanced nitrogen removal from landfill leachate DOI

Pei Yang,

Zhaozhi Wang, Chenguang Zhang

et al.

Bioresource Technology, Journal Year: 2025, Volume and Issue: unknown, P. 132257 - 132257

Published: Feb. 1, 2025

Language: Английский

Citations

0
Performance and kinetic analysis of biogas production from co‐digestion of landfill leachate with pineapple peel in batch experiments DOI

Souwalak Jaroenpoj,

Qi Yu,

James Ness

et al.

Biofuels Bioproducts and Biorefining, Journal Year: 2024, Volume and Issue: unknown

Published: Nov. 22, 2024

Abstract This study examines the co‐digestion of landfill leachate (LFL) with pineapple peel, focusing on biogas production. The was conducted a lab‐scale batch anaerobic digester using 30 L working volume completely mixed reactor at 35 °C to investigate monodigestion and peel their three different mixing ratios. results all experiments in were fitted first‐order kinetic models compare behavior batches through rate constants ( k ). As expected, digestion 25 achieved yield 38 kg −1 volatile solids (VS) consumed VS removal efficiency 30%, both markedly lower than those 3 per m tap water (513 80% efficiency). leachate, which had fixed L, 1, 2, −3 . showed that 2 highest 431 approximately 90% chemical oxygen demand (COD) stable conditions reactor. kinetics equation selected characterize able describe processes experiments. ) 0.25, 0.22, 0.18 day for

Language: Английский

Citations

0