https://ogma.newcastle.edu.au/vital/access/ /manager/Index ${session.getAttribute("locale")} 5 https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:40760 Wed 28 Feb 2024 14:59:36 AEDT ]]> https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:34989 Wed 09 Jun 2021 16:04:03 AEST ]]> https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:49849 Wed 06 Mar 2024 15:04:13 AEDT ]]> https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:47623 2 concentration in the flue gas on denitrification performances of EG-TBAB DESs have been investigated. The highest denitrification efficiency and capacity were achieved using EG to TBAB molar ratio of 50:1 at an operation temperature of 50 °C. The O₂ partial pressure in the flue gas showed no noticeable effects on NO absorption in EG-TBAB DESs. EG-TBAB DESs maintain high denitrification stability after five absorption–desorption cycles. The calculated absorption equilibrium constant (K⁰) and Henry’s law constant (H) showed that EG-TBAB DESs exhibited high absorption capacity for NO molecules, indicating that they are applicable in industrial denitrification processes. The kinetics analysis of NO absorption in EG-TBAB DESs indicated that EG-TBAB DESs could effectively absorb NO and the absorption of NO was strongly influenced by mass transfer.]]> Tue 24 Jan 2023 13:55:42 AEDT ]]> https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:55404 Mon 27 May 2024 12:04:23 AEST ]]>