https://nova.newcastle.edu.au/vital/access/ /manager/Index ${session.getAttribute("locale")} 5 https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:28040 e coal-fired power plant in New South Wales, Australia, for oxy-fuel conversion using integrated chemical looping air separation (ICLAS) technology and cryogenic air separation unit (CASU). The key objectives of this study are to (i) investigate and compare the detailed integration options for oxy-fuel conversion using ICLAS and CASU and (ii) determine the technical merits of the above integration options and the conditions at which the technologies become economically feasible. The study produced scientific evidence that confirms the viability of the CLAS process from both technical and economic points of view under certain conditions. The detailed technical analysis revealed that ICLAS with natural gas integration is energy-efficient compared to CASU running on parasitic load. This is primarily due to the fact that ICLAS needs less auxiliary power compared to CASU. Despite the fact that ICLAS natural gas integration has resulted in higher efficiencies than CASU running on parasitic load, from a series of detailed economic analyses, it was observed that both ICLAS and CASU may not be viable under the present operating and economic conditions. Nevertheless, from sensitivity analysis, it was concluded that ICLAS can become feasible if economic conditions are improved, e.g., a low natural gas market price (<$3.5/GJ), a high electricity wholesale price (>$59/MWh), and/or a high carbon tax (>$33/tonne).]]> Wed 31 Aug 2022 08:48:11 AEST ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:45153 Wed 28 Feb 2024 14:54:59 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:15846 Wed 11 Apr 2018 12:14:38 AEST ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:16484 Wed 11 Apr 2018 11:35:10 AEST ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:43917 Wed 05 Oct 2022 09:00:26 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:48426 Thu 16 Mar 2023 14:11:08 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:8047 Sat 24 Mar 2018 08:35:05 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:11959 Sat 24 Mar 2018 08:09:35 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:20823 Sat 24 Mar 2018 08:05:54 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:20979 Sat 24 Mar 2018 07:54:21 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:20980 Sat 24 Mar 2018 07:54:20 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:28023 Sat 24 Mar 2018 07:40:59 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:28659 Cu⁺ > Cu²⁺. Fe₃O₄ was believed to be the active phase in Fe catalyst. The oxygen and char-supported metal catalysts significantly promoted C/NO reaction, and therefore may lead to a lower operation temperature of NOₓ removal.]]> Sat 24 Mar 2018 07:37:12 AEDT ]]> https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:24611 Sat 24 Mar 2018 07:11:55 AEDT ]]>