ORCID Profile
0000-0002-2761-880X
Current Organisation
Monash University
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In Research Link Australia (RLA), "Research Topics" refer to ANZSRC FOR and SEO codes. These topics are either sourced from ANZSRC FOR and SEO codes listed in researchers' related grants or generated by a large language model (LLM) based on their publications.
Membrane and Separation Technologies | Chemical Engineering | Non-automotive Combustion and Fuel Engineering (incl. Alternative/Renewable Fuels) | Chemical and thermal processes in energy and combustion | Materials Engineering | Waste management reduction reuse and recycling | Chemical engineering | Renewable Power and Energy Systems Engineering (excl. Solar Cells) | Mineralogy and Crystallography | Catalytic Process Engineering | Carbon Capture Engineering (excl. Sequestration) | Food Chemistry and Molecular Gastronomy (excl. Wine) | Structural Biology (incl. Macromolecular Modelling) | Other Chemical Sciences | Functional Materials | Combustion And Fuel Engineering | Polymers and Plastics | Metals and Alloy Materials | Powder and particle technology | Chemical engineering design | Bioinorganic Chemistry | Bio-Remediation | Structural Chemistry and Spectroscopy | Chemotherapy | Inorganic Geochemistry | Industrial Chemistry | Nanomaterials | Medical Biochemistry and Metabolomics | Chemical Engineering not elsewhere classified | Soil Chemistry (excl. Carbon Sequestration Science) | Crop and Pasture Biochemistry and Physiology | Medical Biochemistry: Proteins and Peptides (incl. Medical Proteomics) | Medical Biochemistry: Inorganic Elements and Compounds | Geology not elsewhere classified | Analytical Biochemistry | Atomic and Molecular Physics
Transformation of Coal into Gaseous Fuels | Biofuel (Biomass) Energy | Expanding Knowledge in the Physical Sciences | Expanding Knowledge in Engineering | Management of Liquid Waste from Mineral Resource Activities (excl. Water) | Management of Solid Waste from Energy Activities | Management of Solid Waste from Mineral Resource Activities | Management of Greenhouse Gas Emissions from Electricity Generation | Industry | Inorganic Industrial Chemicals | Organic Industrial Chemicals (excl. Resins, Rubber and Plastics) | Environmentally Sustainable Manufacturing not elsewhere classified | Production of Biofuels (Biomass) | Mining and Extraction of Precious (Noble) Metal Ores | Expanding Knowledge in History and Archaeology | Energy Transformation not elsewhere classified | Climate Change Mitigation Strategies | Coal—other purposes | Coal—electricity | Transformation of Coal into Liquid Fuels | Expanding Knowledge in the Medical and Health Sciences | Industrial Energy Conservation and Efficiency | Human Pharmaceutical Treatments (e.g. Antibiotics) | Expanding Knowledge in the Environmental Sciences | Expanding Knowledge in the Earth Sciences | Expanding Knowledge in the Chemical Sciences | Industrial Chemicals and Related Products not elsewhere classified | Expanding Knowledge in the Agricultural and Veterinary Sciences | Expanding Knowledge in the Biological Sciences |
Publisher: American Chemical Society (ACS)
Date: 05-01-2011
DOI: 10.1021/EF1008192
Publisher: Elsevier BV
Date: 10-2015
Publisher: Elsevier BV
Date: 10-2015
Publisher: American Chemical Society (ACS)
Date: 07-2011
DOI: 10.1021/ES200545E
Abstract: Speciation of chromium (Cr) in the fly ash collected from oxy-firing of Victorian brown coal has been reported for the first time to address the potential formation of toxic Cr(VI) and the variation of the quantities of Cr(III)-bearing species with flue gas composition. Synchrotron-based X-ray absorption near-edge structure (XANES) was employed for Cr speciation. Apart from a pure O(2)/CO(2) mixture (27/73, v/v) versus air, the O(2)/CO(2) mixtures doped with SO(2), HCl, and steam in idually or together to simulate real flue gas have also been tested. Under all of the conditions tested here, the fractions of Cr(VI) in the fly ashes are insignificant, constituting no more than 5% of the total Cr. The test of Cr-doped brown coal in pyrolysis further confirmed that the Cr(VI) formation preferentially occurred through a local oxidation of Cr(III) at the oxygen-containing functions sites within coal matrix, rather than through an oxidation by external bulk O(2). This reaction is also highly temperature-dependent and slower than the interaction between Cr(III) and other metals such as iron oxide. Increasing temperature to 1000 °C inhibited the oxidation of Cr(IIII) to Cr(VI). Shifting the combustion gas from air to O(2)/CO(2) exerted little effect on the Cr(VI) formation. Instead, the formation of iron chromite (FeCr(2)O(4)) was facilitated in O(2)/CO(2), probably due to a strong reducing microenvironment formed by the CO(2) gasification reaction within the char matrix. The accumulation of HCl in flue gas favored the vaporization of chromium as gaseous chloride/oxychloride, as expected. The coexistence of SO(2) inhibited this phenomenon by promoting the formation of sulfate. The presence of steam was even beneficial for the inhibition of water-soluble Cr sulfate through stabilizing the majority of Cr into alumino-silicate which is in the slagging phase.
Publisher: Elsevier BV
Date: 10-2010
Publisher: Elsevier BV
Date: 2007
Publisher: Elsevier BV
Date: 03-2015
Publisher: American Chemical Society (ACS)
Date: 23-09-2013
DOI: 10.1021/EF400930E
Publisher: Royal Society of Chemistry (RSC)
Date: 2019
DOI: 10.1039/C9EE00692C
Abstract: Efficient solar steam generation and concurrent salt harvesting from saline water were achieved with both continuous operation and long-term stability.
Publisher: American Chemical Society (ACS)
Date: 14-11-2018
Publisher: Elsevier BV
Date: 2015
Publisher: Elsevier BV
Date: 2015
Publisher: Elsevier BV
Date: 09-2020
Publisher: Elsevier BV
Date: 2020
Publisher: Elsevier BV
Date: 09-2012
Publisher: Royal Society of Chemistry (RSC)
Date: 2020
DOI: 10.1039/D0EN00840K
Abstract: Reduced rubidium tungstate nanorods were employed to activate peroxydisulfate under alkaline conditions for bisphenol A degradation.
Publisher: Elsevier BV
Date: 07-2022
Publisher: American Chemical Society (ACS)
Date: 23-09-2014
DOI: 10.1021/EF5014314
Publisher: Elsevier BV
Date: 2015
Publisher: American Chemical Society (ACS)
Date: 27-02-2019
Publisher: American Chemical Society (ACS)
Date: 23-09-2019
Publisher: National Library of Serbia
Date: 2014
Abstract: The hydrolysis of corn stover using hydrochloric acid was studied. The kinetic parameters of the mathematical models for predicting the yields of xylose, glucose, furfural and acetic acid were obtained, and the corresponding xylose generation activation energy of 100 kJ/mol was determined. The characterization of corn stover using with different techniques during hydrolysis indicated an effective removal of xylan and the slightly alteration on the structures of cellulose and lignin. A 23five levels Central Composite Design (CCD) was used to develop a statistical model for the optimization of process variables including acid concentration, pretreatment temperature and time. The optimum conditions determined by this model were found to be 108?C for 80 minutes with acid concentration of 5.8%. Under these conditions, the maximised results are the following: xylose 19.93 g/L, glucose 1.2 g/L, furfural 1.5 g/L, acetic acid 1.3 g/L. The validation of the model indicates a good agreement between the experimental results and the predicted values.
Publisher: American Chemical Society (ACS)
Date: 18-07-2013
DOI: 10.1021/EF400032T
Publisher: Elsevier BV
Date: 03-2021
Publisher: Wiley
Date: 15-04-2008
DOI: 10.1002/AIC.11474
Publisher: Elsevier BV
Date: 07-2002
Publisher: Elsevier BV
Date: 03-2020
Publisher: Elsevier BV
Date: 05-2008
Publisher: Springer Science and Business Media LLC
Date: 21-05-2018
Publisher: Royal Society of Chemistry (RSC)
Date: 2021
DOI: 10.1039/D1EE00247C
Abstract: This review summarizes the recent advances about noble-metal single-atom catalysts in thermocatalysis, electrocatalysis, and photocatalysis.
Publisher: Elsevier BV
Date: 09-2020
Publisher: Elsevier BV
Date: 07-2004
Publisher: Elsevier BV
Date: 2011
Publisher: Elsevier BV
Date: 2013
Publisher: The Japan Institute of Energy
Date: 2006
DOI: 10.3775/JIE.85.762
Publisher: Springer Science and Business Media LLC
Date: 04-07-2023
DOI: 10.1038/S41467-023-39478-2
Abstract: Noble metals have been extensively employed in a variety of hydrotreating catalyst systems for their featured functionality of hydrogen activation but may also bring side reactions such as undesired deep hydrogenation. It is crucial to develop a viable approach to selectively inhibit side reactions while preserving beneficial functionalities. Herein, we present modifying Pd with alkenyl-type ligands that forms homogeneous-like Pd-alkene metallacycle structure on the heterogeneous Pd catalyst to achieve the selective hydrogenolysis and hydrogenation. Particularly, a doped alkenyl-type carbon ligand on Pd-Fe catalyst is demonstrated to donate electrons to Pd, creating an electron-rich environment that elongates the distance and weakens the electronic interaction between Pd and unsaturated C of the reactants roducts to control the hydrogenation chemistry. Moreover, high H 2 activation capability is maintained over Pd and the activated H is transferred to Fe to facilitate C-O bond cleavage or directly participate in the reaction on Pd. The modified Pd-Fe catalyst displays comparable C-O bond cleavage rate but much higher selectivity ( %) than the bare Pd-Fe ( %) in hydrotreating of diphenyl ether (DPE, modelling the strongest C-O linkage in lignin) and enhanced ethene selectivity ( %) in acetylene hydrogenation. This work sheds light on the controlled synthesis of selective hydrotreating catalysts via mimicking homogeneous analogues.
Publisher: American Chemical Society (ACS)
Date: 19-01-2021
Publisher: American Chemical Society (ACS)
Date: 14-07-2014
DOI: 10.1021/EF500981K
Publisher: Royal Society of Chemistry (RSC)
Date: 2021
DOI: 10.1039/D1TA03963F
Abstract: An oxygen vacancy (V O )-rich Co 3 O 4 @carbon composite was employed to activate peroxymonosulfate for bisphenol A degradation.
Publisher: Elsevier BV
Date: 2013
Publisher: Informa UK Limited
Date: 2015
DOI: 10.1252/JCEJ.14WE224
Publisher: American Chemical Society (ACS)
Date: 20-01-2015
DOI: 10.1021/EF502287C
Publisher: Elsevier BV
Date: 06-2020
Publisher: American Chemical Society (ACS)
Date: 31-08-2010
DOI: 10.1021/EF100314K
Publisher: American Chemical Society (ACS)
Date: 03-01-2019
Publisher: Springer Singapore
Date: 2016
Publisher: Wiley
Date: 31-12-2022
Abstract: Single‐atom catalysts (SACs) have shown great potential in the electrochemical oxygen reduction reaction (ORR) toward hydrogen peroxide (H 2 O 2 ) production. However, current studies are mainly focused on 3d transition‐metal SACs, and very little attention has been paid to 5d SACs. Here, a new kind of W SAC anchored on a porous O, N‐doped carbon nanosheet (W 1 /NO‐C) is designed and prepared via a simple coordination polymer‐pyrolysis method. A unique local structure of W SAC, terdentate W 1 N 1 O 2 with the coordination of two O atoms and one N atom, is identified by the combination of aberration‐corrected scanning transmission electron microscopy, X‐ray photoelectron spectroscopy and X‐ray absorption fine structure spectroscopy. Remarkably, the as‐prepared W 1 /NO‐C catalyzes the ORR via a 2e – pathway with high onset potential, high H 2 O 2 selectivity in the wide potential range, and excellent operation durability in 0.1 m KOH solution, superior to most of state‐of‐the‐art H 2 O 2 electrocatalysts ever reported. Theoretical calculations reveal that the C atoms adjacent to O in the W 1 N 1 O 2 ‐C moiety are the most active sites for the 2e – ORR to H 2 O 2 with the optimal binding energy of the HOO* intermediate. This work opens up a new opportunity for the development of high‐performance W‐based catalysts for electrochemical H 2 O 2 production.
Publisher: Elsevier BV
Date: 07-2004
Publisher: American Chemical Society (ACS)
Date: 15-05-2010
DOI: 10.1021/ES1001538
Abstract: Understanding the conversion of coal-N during gasification is an important part of the development of gasification-based power generation technologies to reduce NO(x) emissions from coal utilization. This study investigated the conversion of coal-N in the presence of NO during the gasification of three rank-ordered coals and their chars in steam and low-concentration O(2). Our results show that NO can be incorporated into the char structure during gasification. The inherent char-N and the N incorporated into the char from NO-char reactions behave very similarly during gasification. During the gasification in steam, significant amounts of HCN and NH(3) can be formed from the incorporated N structure in char, especially for the relatively "aged" chars, mainly due to the availability of abundant H radicals on the char surface during the gasification in steam. During the gasification in 2000 ppm O(2), the formation of HCN or NH(3) from the N structures in char, including those incorporated into the char from the NO-char reactions, was not a favored route of reaction mainly due to the lack of H on char surface in the presence of O(2).
Publisher: Elsevier BV
Date: 11-2020
Publisher: Elsevier BV
Date: 09-2021
Publisher: Inderscience Publishers
Date: 2007
Publisher: Springer Singapore
Date: 2016
Publisher: Elsevier BV
Date: 2006
Publisher: Elsevier BV
Date: 2021
Publisher: American Chemical Society (ACS)
Date: 24-12-2006
DOI: 10.1021/EF060419W
Publisher: American Chemical Society (ACS)
Date: 07-03-2012
DOI: 10.1021/ES204255H
Abstract: Through the use of synchrotron XANES and Cr-doped brown coal, extensive efforts have been made to clarify the volatility of organically bound Cr during oxy-fuel combustion and the mode of occurrence and leachability of Cr in resulting fly ashes. As the continuation of our previous study using raw coal, the Cr-doped coal has been tested in this study to improve the signal-to-noise ratio for Cr K-edge XANES spectra, and hence the accuracy for Cr(VI) quantification. As has been confirmed, the abundant CO(2) as a balance gas for oxy-firing has the potential to inhibit the decomposition of organically bound Cr, thereby favoring its retention in solid ash. It also has the potential to promote the oxidation of Cr(III) to Cr(VI) to a minor extent. Increasing the oxygen partial pressure, particularly in the coexistence of HCl in flue gas, favored the oxidation of Cr(III) into gaseous Cr(VI)-bearing species such as CrO(2)Cl(2). Regarding the solid impurities including Na(2)SO(4) and CaO, Na(2)SO(4) has proven to preferentially capture the Cr(III)-bearing species at a low furnace temperature such as 600 °C. Its promoting effect on the oxidation of Cr(III) to Cr(VI), although thermodynamically available at the temperatures examined here, is negligible in a lab-scale drop tube furnace (DTF), where the particle residence time is extremely short. In contrast, CaO has proven facilitating the capture of Cr(VI)-bearing species particularly oxychloride vapors at 1000 °C, forming Ca chromate with the formulas of CaCrO(4) and Ca(3)(CrO(4))(2) via a direction stabilization of Cr(VI) oxychloride vapor by CaO particle or an indirect oxidation of Cr(III) via the initial formation of Ca chromite. The fly ash collected from the combustion of Cr-doped coal alone has a lower water solubility (i.e., 58.7%) for its Cr(VI) species, due to the formation of Ba/Pb chromate and/or the incorporation of Cr(VI) vapor into a slagging phase which is water-insoluble. Adding CaO to coal increased the water-solubility of both Cr(VI) and Cr(III) by forming Ca chromite and chromate, respectively.
Publisher: Elsevier BV
Date: 05-2019
Publisher: American Chemical Society (ACS)
Date: 21-01-2010
DOI: 10.1021/EF900463R
Publisher: Informa UK Limited
Date: 2003
DOI: 10.1252/JCEJ.36.759
Publisher: American Chemical Society (ACS)
Date: 05-02-2014
DOI: 10.1021/IE402600P
Publisher: Elsevier BV
Date: 2015
Publisher: American Chemical Society (ACS)
Date: 12-06-2008
DOI: 10.1021/EF800127G
Publisher: Elsevier BV
Date: 2009
Publisher: Elsevier BV
Date: 2011
Publisher: Royal Society of Chemistry (RSC)
Date: 2020
DOI: 10.1039/D0TA04491A
Abstract: Benefiting from the unique structure and composition, a superior hybrid composed of RuCo alloy bimodal nanoparticles embedded in N-doped carbon exhibits exceptional HER activities in all pH conditions, outperforming the benchmark Pt/C catalyst.
Publisher: Elsevier BV
Date: 10-2013
DOI: 10.1016/J.JHAZMAT.2013.07.023
Abstract: The thermodynamics underpinning the interaction of Cr-bearing species with basic metal oxides, i.e. K2O, Fe2O3, MgO and CaO, during the air and oxy-fuel combustion of coal have been examined. The synchrotron-based X-ray adsorption near-edge spectroscopy (XANES) was used for Cr speciation. For the oxides tested, Cr(VI) formation is dominated by the reduction potential of the metals. The oxides of Ca(2+) with high reduction potential favored the oxidation of Cr(III), same for K(+). The other two basic metals, Fe2O3 and MgO with lower reduction potentials reacted with Cr(III) to form the corresponding chromites at the temperatures above 600°C. Coal combustion experiments in drop-tube furnace have confirmed the rapid capture of Cr vapors, either trivalent or hexavalent, by CaO into solid ash. The existence of HCl in flue gas favored the vaporization of Cr as CrO2Cl2, which was in turn captured by CaO into chromate. Both Fe2O3 and MgO exhibited less capability on scavenging the Cr(VI) vapor. Particularly, MgO alone exhibited a low capability for capturing the vaporized Cr(III) vapors. However, its co-existence with CaO in the furnace inhibited the Cr(VI) formation. This is beneficial for minimizing the toxicity of Cr in the coal combustion-derived fly ash.
Publisher: Elsevier BV
Date: 04-2011
Publisher: American Chemical Society (ACS)
Date: 25-09-2012
DOI: 10.1021/IE300747M
Publisher: American Chemical Society (ACS)
Date: 04-05-2006
DOI: 10.1021/EF050429H
Publisher: Elsevier BV
Date: 10-2015
Publisher: Elsevier BV
Date: 11-2004
Publisher: American Chemical Society (ACS)
Date: 12-07-2013
DOI: 10.1021/EF400744U
Publisher: Elsevier BV
Date: 07-2015
Publisher: Springer Science and Business Media LLC
Date: 26-04-2020
Publisher: American Chemical Society (ACS)
Date: 09-12-2019
Publisher: American Chemical Society (ACS)
Date: 16-02-2008
DOI: 10.1021/EF700610B
Publisher: Elsevier BV
Date: 11-2010
Publisher: Elsevier BV
Date: 02-2021
Publisher: Elsevier BV
Date: 2011
Publisher: Elsevier BV
Date: 2013
Publisher: American Chemical Society (ACS)
Date: 09-06-2015
Abstract: We use in situ high-temperature X-ray diffraction (HT-XRD), ex-situ XRD and synchrotron X-ray absorption near edge structure spectroscopy (XANES) to derive fundamental insights into mechanisms of chromium oxidation during combustion of solid fuels. To mimic the real combustion environment, mixtures of pure eskolaite (Cr(3+)2O3), lime (CaO) and/or kaolinite [Al2Si2O5(OH)4] have been annealed at 600-1200 °C in air versus 1% O2 diluted by N2. Our results confirm for the first time that (1) the optimum temperature for Cr(6+) formation is 800 °C for the coexistence of lime and eskolaite (2) upon addition of kaolinite into oxide mixture, the temperature required to produce chromatite shifts to 1000 °C with a remarkable reduction in the fraction of Cr(6+). Beyond 1000 °C, transient phases are formed that bear Cr in intermediate valence states, which convert to different species other than Cr(6+) in the cooling stage (3) of significance to Cr mobility from the waste products generated by combustion, chromatite formed at >1000 °C has a glassy disposition that prevents its water-based leaching and (4) Increasing temperature facilitates the migration of eskolaite particles into bulk lime and enhances the extent to which Cr(3+) is oxidized, thereby completing the oxidation of Cr(3+) to Cr(6+) within 10 min.
Publisher: Elsevier BV
Date: 07-2013
Publisher: American Chemical Society (ACS)
Date: 23-01-2007
DOI: 10.1021/EF060308X
Publisher: Elsevier BV
Date: 03-2018
Publisher: Elsevier BV
Date: 07-2006
Publisher: Elsevier BV
Date: 2013
Publisher: Elsevier BV
Date: 05-2021
Publisher: Elsevier BV
Date: 10-2021
Publisher: Springer Science and Business Media LLC
Date: 10-08-2020
Publisher: Elsevier BV
Date: 02-2003
Publisher: Elsevier BV
Date: 08-2022
DOI: 10.1016/J.JHAZMAT.2022.129187
Abstract: Concerning the emissions of hydrogen cyanide (HCN) and other N-bearing air pollutants from the fluid catalytic cracking (FCC) regeneration units, this paper has conducted a comprehensive testing and surface characterisation of four industrial spent catalysts, aged catalysts and hard coke s le in three different schemes, Ar-TPD, O
Publisher: Wiley
Date: 02-09-2014
DOI: 10.1002/EP.11828
Publisher: Elsevier BV
Date: 04-2004
Publisher: Elsevier BV
Date: 11-2011
Publisher: Wiley
Date: 22-10-2020
Publisher: Elsevier BV
Date: 05-2004
Publisher: Elsevier BV
Date: 03-2022
Publisher: Elsevier BV
Date: 06-2016
Publisher: Elsevier BV
Date: 11-2019
Publisher: Elsevier BV
Date: 04-2006
DOI: 10.1016/J.JENVMAN.2005.06.006
Abstract: This study examines slag, fly ash, and deposited particles during melting of dewatered sewage sludge in a pilot plant. In addition, the chemical composition of particles in flue gas was simulated using a thermodynamics program, namely FACTSage 5.2. The results showed that the main components of slag were Al, Fe, Ca, P and Si the minor components were Na, K, Mg, Cu, and Zn. The main chemical compound of slag was Ca4(Mg,Fe)5(PO4)6. For fly ash particles, heavy metals with the highest concentrations were in the order of Zn and As, Pb, Cu, and Cd, respectively. For non-heavy metals, Al, Fe and P were also found in significant amounts. The majority of deposited particles were composed of elements of Zn, P, S, Na, Fe, Al, Si, and Ca and such chemical compounds as Zn3(PO4)2, AlPO4, FePO4 and Fe(OH)3 while the minority consisted of elements of As, Cu, and Pb. Moreover, the compositions of deposited particles in each chamber differed due to different flue gas temperatures inside. In the secondary chamber at 760 degrees C, the amounts of Fe and Al were higher than Zn, whereas, in the other chambers (600-400 degrees C), the amount of Zn was higher. In other words, at the lower temperature the deposition of Zn was higher than the deposition of Fe and Al. In the water cooling section, volatile elements (i.e. Zn, As, Cu, Pb) were found in the highest concentrations due to a big difference in temperature between the wall surface and flue gas. From the simulation results, most of the elements in the gas phase were found to be chloride compounds, whereas those in the solid phase were in the form of oxide, sulfate, and phosphate compounds.
Publisher: Elsevier BV
Date: 09-2008
Publisher: Elsevier BV
Date: 03-2012
DOI: 10.1016/J.JHAZMAT.2012.01.053
Abstract: The use of an industry waste, brown coal fly ash collected from the Latrobe Valley, Victoria, Australia, has been tested for the post-combustion CO(2) capture through indirect minersalization in acetic acid leachate. Upon the initial leaching, the majority of calcium and magnesium in fly ash were dissolved into solution, the carbonation potential of which was investigated subsequently through the use of a continuously stirred high-pressure autoclave reactor and the characterization of carbonation precipitates by various facilities. A large CO(2) capture capacity of fly ash under mild conditions has been confirmed. The CO(2) was fixed in both carbonate precipitates and water-soluble bicarbonate, and the conversion between these two species was achievable at approximately 60°C and a CO(2) partial pressure above 3 bar. The kinetic analysis confirmed a fast reaction rate for the carbonation of the brown coal ash-derived leachate at a global activation energy of 12.7 kJ/mol. It is much lower than that for natural minerals and is also very close to the potassium carbonate iperazine system. The CO(2) capture capacity of this system has also proven to reach maximum 264 kg CO(2)/ton fly ash which is comparable to the natural minerals tested in the literature. As the fly ash is a valueless waste and requires no comminution prior to use, the technology developed here is highly efficient and energy-saving, the resulting carbonate products of which are invaluable for the use as additive to cement and in the paper and pulp industry.
Publisher: Elsevier BV
Date: 11-2012
DOI: 10.1016/J.TALANTA.2012.09.037
Abstract: In this paper, microwave digestion conditions have been optimised to achieve complete recoveries for the ash-forming inorganic elements in coal and coal combustion fly ash, during the analysis by inductively coupled plasma optical emission spectroscopy (ICP-OES). The elements analysed include six major (Al, Ca, Fe, K, Mg and Na) and twelve trace (As, Ba, Be, Co, Cr, Cu, Li, Mn, Ni, Pb, Sr and V). Seven reference s les have been tested, including two standard coal references, SRM1632c and SARM19, their corresponding high-temperature ashes (HTAs), and three coal fly ash references, SRM1633c, SRM2690 and BCR38. The recoveries of in idual elements in these s les have been examined intensively, as a function of the amount of hydrofluoric acid (HF, 0-2.0 ml), microwave power (900 W vs. 1200 W) and s le mass (0.05 g vs. 0.1 g). As have been confirmed, the recoveries of these in idual elements varied significantly with the microwave digestion condition, elemental type and s le property. For the coal references and their HTAs, the use of HF can be ruled out for most of the elements, except K associated with feldspar, Pb and V. In particular, the recovery of Pb in coal is highly s le-specific and thus unpredictable. The majority of elements in fly ash references require the use of 0.1-0.2 ml HF for a complete recovery. Al in fly ash is the only exceptional element which gave incomplete recoveries throughout, suggesting the use of a complementary technique for its quantification. As has proven to be the only element inconsequential of s le type and digestion conditions, achieving complete recoveries for all cases. On the power parameter, using a higher power such as 1200 W is critical, which has proved to be an ultimatum for the recovery of certain elements, especially in fly ash. Halving s le mass from 0.1 g to 0.05 g was also found to be insignificant.
Publisher: Elsevier BV
Date: 08-2022
Publisher: Elsevier BV
Date: 2015
Publisher: Wiley
Date: 05-10-2019
DOI: 10.1002/EP.13053
Publisher: Elsevier BV
Date: 2011
Publisher: Elsevier BV
Date: 12-2018
Publisher: Elsevier BV
Date: 02-2020
Publisher: Elsevier BV
Date: 02-2021
Publisher: The Japan Institute of Energy
Date: 2005
DOI: 10.3775/JIE.84.359
Publisher: Elsevier BV
Date: 12-2012
Publisher: American Chemical Society (ACS)
Date: 29-05-2014
DOI: 10.1021/EF500618R
Publisher: American Chemical Society (ACS)
Date: 22-05-2014
DOI: 10.1021/EF5003777
Publisher: American Chemical Society (ACS)
Date: 29-01-2018
Publisher: Elsevier BV
Date: 10-2015
Publisher: Elsevier BV
Date: 10-2008
Publisher: Wiley
Date: 22-09-2009
DOI: 10.1002/AIC.11922
Publisher: Elsevier BV
Date: 06-2022
Publisher: American Chemical Society (ACS)
Date: 29-11-2006
DOI: 10.1021/EF060024C
Publisher: Elsevier BV
Date: 02-2013
Publisher: Elsevier BV
Date: 06-2022
Publisher: Elsevier BV
Date: 2009
Publisher: American Chemical Society (ACS)
Date: 25-07-2012
DOI: 10.1021/EF300804E
Publisher: American Chemical Society (ACS)
Date: 23-01-2007
DOI: 10.1021/EF0603075
Publisher: American Chemical Society (ACS)
Date: 27-02-2019
Publisher: American Chemical Society (ACS)
Date: 17-07-2012
DOI: 10.1021/EF3005459
Publisher: American Chemical Society (ACS)
Date: 13-10-2015
Publisher: Elsevier BV
Date: 06-2019
Publisher: Elsevier BV
Date: 06-2011
Publisher: Elsevier BV
Date: 08-2020
Publisher: The Japan Institute of Energy
Date: 2005
DOI: 10.3775/JIE.84.767
Start Date: 01-2010
End Date: 01-2014
Amount: $686,400.00
Funder: Australian Research Council
View Funded ActivityStart Date: 10-2017
End Date: 12-2020
Amount: $469,000.00
Funder: Australian Research Council
View Funded ActivityStart Date: 09-2019
End Date: 12-2023
Amount: $390,000.00
Funder: Australian Research Council
View Funded ActivityStart Date: 09-2023
End Date: 09-2026
Amount: $747,270.00
Funder: Australian Research Council
View Funded ActivityStart Date: 12-2011
End Date: 12-2012
Amount: $800,000.00
Funder: Australian Research Council
View Funded ActivityStart Date: 2013
End Date: 12-2014
Amount: $350,000.00
Funder: Australian Research Council
View Funded ActivityStart Date: 01-2025
End Date: 01-2029
Amount: $4,955,854.00
Funder: Australian Research Council
View Funded ActivityStart Date: 01-2012
End Date: 12-2013
Amount: $300,000.00
Funder: Australian Research Council
View Funded ActivityStart Date: 12-2017
End Date: 12-2023
Amount: $4,000,000.00
Funder: Australian Research Council
View Funded Activity