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

и другие.

Biofuels Bioproducts and Biorefining, Год журнала: 2024, Номер unknown

Опубликована: Ноя. 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

Язык: 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

и другие.

Bioresource Technology, Год журнала: 2025, Номер unknown, С. 132257 - 132257

Опубликована: Фев. 1, 2025

Язык: Английский

Процитировано

1

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

и другие.

Biofuels Bioproducts and Biorefining, Год журнала: 2024, Номер unknown

Опубликована: Ноя. 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

Язык: Английский

Процитировано

0