https://nova.newcastle.edu.au/vital/access/ /manager/Index ${session.getAttribute("locale")} 5 Microstructural and associated chemical changes during the composting of a high temperature biochar: Mechanisms for nitrate, phosphate and other nutrient retention and release https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:36405 Wed 24 May 2023 09:45:52 AEST ]]> The electrochemical properties of biochars and how they affect soil redox properties and processes https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:23079 Wed 11 Apr 2018 09:21:28 AEST ]]> Sodium-ion battery anodes from carbon depositions https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:49071 Wed 03 May 2023 16:08:05 AEST ]]> Optimal pre-treatment of a Ni-11Fe-10Cu anode for efficient molten salt electrolysis of carbon dioxide: Toward net-zero emission manufacturing https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:54534 Tue 27 Feb 2024 20:42:12 AEDT ]]> A New Approach to Turbostratic Carbon Production Via Thermal Salt-Assisted Treatment of Graphite https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:50414 2CO3: 43.5%, Na2CO3: 31.5%, K2CO3: 25%) during slow temperature ramping rates (5 °C/min) under N2 at temperatures above 750 °C. Initial findings suggest that approximately 50 wt% of graphite experiences interlayer expansion. The conventional d spacing of 0.34 nm is modified to a range of intervals between 0.41 nm and 1.22 nm. As a consequence of high operational temperature (800 °C), cations (Li+, Na+ and K+) as well as potentially the anion (CO32–) intercalate between graphitic layers and overcome Van der Waal force between layers. Employing a pressurized N2 environment of 5 bar and 10 bar successfully controls carbonate vaporization and decomposition, as well as inducing ordered layer manipulation to exfoliate more graphite planes from the edges towards deeper levels of the particles. Exploring parameters of both carbonate loading and treatment time in addition to pressure demonstrate that this work opens up a rich selection of parameters that can be used to produce carbons with tuned properties from graphite.]]> Tue 25 Jul 2023 17:58:35 AEST ]]> Reclaiming water from a direct air capture plant using vacuum membrane distillation – A bench-scale study https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:52767 Tue 14 Nov 2023 15:12:48 AEDT ]]> Influence of selected coal contaminants on graphitic carbon electro-oxidation for application to the direct carbon fuel cell https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:20725 Sat 24 Mar 2018 08:00:20 AEDT ]]> Dynamic electrodeposition of manganese dioxide: temporal variation in the electrodeposition mechanism https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:24734 3+ intermediate is a key feature of this electrodeposition mechanism, the formation of which is dependent on the substrate, which in this case is either platinum, MnO₂ or MnOOH. On the platinum surface, for all electrolytes, soluble Mn3+ is produced initially. The stability of this soluble Mn3+ species determines the initial morphology, and rate of change of mechanism for the process. In a neutral electrolyte, nucleation and growth of MnO₂ occurs primarily through the precipitation of a 2D film of MnOOH on the platinum, which rapidly covers the surface. Nucleation in an acidic H₂SO₄ system occurs primarily via a disproportionation route which forms 3D MnO₂ hemispheroids that cover the substrate slowly. Subsequent growth of MnO₂ in both electrolytes then proceeds via formation of a MnOOH film, which is subsequently oxidized in the solid state to form MnO₂. MnOOH oxidation to MnO₂ appears kinetically limited, which is overall a limiting factor in the electrodeposition process.]]> Sat 24 Mar 2018 07:10:58 AEDT ]]> The interplay between ternary molten carbonate and biomaterials during pressurized slow pyrolysis https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:45721 Mon 29 Jan 2024 18:37:58 AEDT ]]> Influence of Growth Parameters on the Electrochemical Performance of Electrodeposited Carbons https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:45397 Mon 29 Jan 2024 18:34:23 AEDT ]]> Thermochemical conversion of biomass in the presence of molten alkali-metal carbonates under reducing environments of N2 and CO2 https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:40921 Mon 29 Jan 2024 17:48:04 AEDT ]]> The impact of carbonate salts on char formation and gas evolution during the slow pyrolysis of biomass, cellulose, and lignin https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:44056 2CO3: 43.5%, Na2CO3: 31.5%, K2CO3: 25% mol), subjected to two different higher heating temperatures (350 °C and 600 °C). It is shown here that the addition of a carbonate eutectic affects char-making reactions through: tar generation modification, changes in the emitted volatile molecules, alteration of surface oxygenate bonds as well as transformation in the morphology of the remnant char. Initial results using Differential Thermal Gravimetric Analysis (DTG) show that, in carbonate treated samples, char yield is increased at both temperatures investigated. In treated cellulose, a reduced temperature onset of mass loss is observed, expected to be from modified depolymerisation and inhibition of levoglucosan formation for samples heated to both 350 °C and 600 °C. Gas analysis by micro-GC proves that carbonate is involved in the cracking of condensable volatiles, which generates a highly porous char structure and increases the emission of non-condensable volatiles. In addition, SEM results for carbonate treated cellulose demonstrate extensive pore generation including both surface and internally generated pores and interconnected tunnel-like structures at higher temperature (600 °C). This was not reflected however in BET results due to the melted salt blocking the available internal porous structure. Improvement in BET results for chars produced at 600 °C was regardless seen on carbonate addition in both biomass (improving from 371 m2 g−1 to 516 m2 g−1) and lignin (improving from 11 m2 g−1 to 209 m2 g−1).]]> Mon 29 Jan 2024 17:46:29 AEDT ]]> State of the climate in 2020 https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:54847 Fri 15 Mar 2024 17:00:44 AEDT ]]> Modification of biochar formation during slow pyrolysis in the presence of alkali metal carbonate additives https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:46145 Eucalyptus pilularis biomass and ternary molten carbonate eutectic [Li2CO3, 43.5%; Na2CO3, 31.5%; and K2CO3, 25% (mole percentage)] in thermogravimetric analysis at three different temperatures, 600, 750, and 900 °C, was studied. These salts affect the slow pyrolysis process, including changes in the volatile release mechanism and the morphology of remnant char material. The initial results show that, in the presence of molten carbonate, biomass particles make bubble-shaped larger particles, which result in less volatile emissions and more char residue. It is suggested that the ternary eutectic has a chemical diluent and catalytic role, particularly in the case of higher salt doping. Results from scanning electron microscopy images give strong evidence that molten carbonates capture volatiles inside swelling carbon particles, which causes the generation of various sizes of pores as well as char-making reactions, and at a higher temperature, the bubble-shaped particles will rupture. Swelling of this nature has previously only been observed clearly in coal precursors; however, this is the first observation in a biomass-based system. Also, at a temperature above 750 °C, decomposition of molten carbonate generates CO2 and carbon/carbonate gasification produces CO as well as a more “activated” biochar.]]> Fri 11 Nov 2022 18:31:02 AEDT ]]> Magnetic carbon formation via in-situ CO₂ capture and electrolysis in a molten carbonate system https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:54173 Fri 09 Feb 2024 14:23:24 AEDT ]]> Electrochemical Ammonia: Power to Ammonia Ratio and Balance of Plant Requirements for Two Different Electrolysis Approaches https://nova.newcastle.edu.au/vital/access/ /manager/Repository/uon:40340 Fri 08 Jul 2022 10:26:31 AEST ]]>