ORCID Profile
0000-0002-7590-6814
Current Organisation
Monash University
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Chemical Engineering | Environmental Technologies | Non-automotive Combustion and Fuel Engineering (incl. Alternative/Renewable Fuels) | Environmental Engineering | Waste management reduction reuse and recycling | Organic Green Chemistry | Carbon Capture Engineering (excl. Sequestration) | Chemical Sciences not elsewhere classified | Membrane and Separation Technologies | Environmental Technologies | Chemical Engineering Not Elsewhere Classified | Timber, Pulp and Paper | Materials Engineering not elsewhere classified | Chemical and thermal processes in energy and combustion | Chemical engineering | Functional Materials | Materials Engineering | Chemical engineering design
Energy transformation not elsewhere classified | Management of Greenhouse Gas Emissions from Electricity Generation | Other | Paper Products (incl. Coated Paper) | Organic Industrial Chemicals (excl. Resins, Rubber and Plastics) | Transformation of Coal into Liquid Fuels | Expanding Knowledge in Technology | Biofuel (Biomass) Energy | Transformation of Coal into Gaseous Fuels | Expanding Knowledge in Engineering | Waste management | Manufactured products not elsewhere classified |
Publisher: Informa UK Limited
Date: 17-08-2015
Publisher: Elsevier BV
Date: 1994
Publisher: Elsevier BV
Date: 02-2016
Publisher: American Chemical Society (ACS)
Date: 29-09-2021
Publisher: American Chemical Society (ACS)
Date: 21-09-2023
Publisher: Elsevier BV
Date: 12-2013
Publisher: Elsevier BV
Date: 07-2012
Publisher: Elsevier BV
Date: 09-2011
Publisher: Elsevier BV
Date: 09-2017
DOI: 10.1016/J.WASMAN.2017.05.011
Abstract: A bench scale, two-stage, thermo-catalytic reactor equipped with a continuous feeding system was used to pyrolyse pure and waste plastics. Experiments using five zeolitic and clay-based catalysts of different forms (pellet and powders) and different plastic feedstocks - virgin HDPE, HDPE w1aste and mixed plastic waste (MPW) were compared to the control experiments - pyrolysis without catalyst. Results indicated that the two pelletized catalysts were the most promising for the conditions employed. Of these two, one with higher acidity and surface area was highly selective for the gasoline fraction (C
Publisher: Elsevier BV
Date: 2013
Publisher: IEEE
Date: 03-2018
Publisher: Elsevier BV
Date: 07-2018
Publisher: Elsevier
Date: 2004
Publisher: Elsevier BV
Date: 08-2015
Publisher: Elsevier BV
Date: 03-2018
Publisher: Elsevier BV
Date: 05-2003
Publisher: Elsevier BV
Date: 2015
Publisher: MDPI AG
Date: 05-11-2021
DOI: 10.3390/EN14217384
Abstract: This study assessed the entrained flow co-gasification characteristics of coal and biomass using thermodynamic equilibrium modelling. The model was validated against entrained flow gasifier data published in the literature. The gasification performance was evaluated under different operating conditions, such as equivalence ratio, temperature, pressure and coal to biomass ratio. It is observed that the lower heating value (LHV) and cold gas efficiency (CGE) increase with increasing temperature until the process reaches a steady state. The effect of pressure on syngas composition is dominant only at non-steady state conditions ( °C). The variation in syngas composition is minor up to the blending of 50% biomass (PB50). However, the PB50 shows a higher LHV and CGE than pure coal by 12%and 18%, respectively. Overall, biomass blending of up to 50% favours gasification performance with an LHV of 12 MJ/kg and a CGE of 78%.
Publisher: Elsevier BV
Date: 06-2018
Publisher: Elsevier BV
Date: 11-2016
Publisher: Elsevier BV
Date: 03-2019
Publisher: Elsevier BV
Date: 09-2012
Publisher: Institute of Electrical and Electronics Engineers (IEEE)
Date: 02-2022
Publisher: American Chemical Society (ACS)
Date: 25-06-2003
DOI: 10.1021/EF020205O
Publisher: Elsevier BV
Date: 11-2006
DOI: 10.1205/PSEP06007
Publisher: Elsevier BV
Date: 04-2018
Publisher: American Chemical Society (ACS)
Date: 25-01-2017
Publisher: Elsevier BV
Date: 09-2023
Publisher: Elsevier BV
Date: 10-2003
Publisher: American Chemical Society (ACS)
Date: 12-01-2015
DOI: 10.1021/SC500777U
Publisher: Elsevier BV
Date: 2009
Publisher: Royal Society of Chemistry (RSC)
Date: 2021
DOI: 10.1039/D0SE01887B
Abstract: In situ synthesis of methane in a single-temperature zone SOEC in the absence of any methanation catalyst is a completely electrochemical phenomenon governed by the thermodynamic equilibrium of various reactions.
Publisher: Elsevier BV
Date: 2016
Publisher: Elsevier BV
Date: 10-2014
Publisher: American Chemical Society (ACS)
Date: 27-11-2012
DOI: 10.1021/EF3016443
Publisher: American Chemical Society (ACS)
Date: 23-05-2019
Publisher: Springer Science and Business Media LLC
Date: 12-01-2016
Publisher: Elsevier BV
Date: 04-2021
Publisher: Elsevier BV
Date: 08-2013
Publisher: MDPI AG
Date: 24-08-2022
Abstract: This study presented an optimisation study of two-stage vapour-phase catalytic glycerol reforming (VPCGR) using response surface methodology (RSM) with a central composite experimental design (CCD) approach. Characterisation through Brunauer–Emmett–Teller analysis (BET), small-angle X-ray scattering (SAXS), scanning electron microscopy coupled with energy dispersive X-ray analysis (SEM-EDX), atomic force microscopy (AFM) and particle X-ray diffraction (PXRD) were carried out to understand the physiochemical activity of the honeycomb morphology CuO/CeO2 catalyst. Notably, in this study, we achieved the desired result of glycerol conversion (94%) and H2 production (81 vol.%) under the reaction condition of Cu species loading (10 wt.%), reaction temperature (823 K), WHSV (2 h−1) and glycerol concentration (15 wt.%). From the RSM analysis, an optimum predicted model for VPCGR was obtained and further integrated into Microsoft Excel and Aspen Plus to perform an energy analysis of the VPCGR plant at a scale of 100 kg h−1 of glycerol feed. As a whole, this study aimed to provide an overview of the technical operation and energy aspect for a sustainable frontier in glycerol reforming.
Publisher: Elsevier BV
Date: 11-2016
Publisher: Elsevier BV
Date: 04-1999
Publisher: Elsevier BV
Date: 2014
Publisher: Wiley
Date: 15-02-2013
DOI: 10.1002/APJ.1722
Publisher: Elsevier BV
Date: 02-2021
Publisher: American Chemical Society (ACS)
Date: 09-05-2019
Publisher: Elsevier BV
Date: 09-2013
Publisher: American Chemical Society (ACS)
Date: 10-05-2016
Publisher: Wageningen Academic Publishers
Date: 11-07-2017
Publisher: Elsevier BV
Date: 03-2012
DOI: 10.1016/J.BIORTECH.2011.12.094
Abstract: Apart from capturing carbon dioxide, fresh water algae can be used to produce biofuel. To assess the energy potential of Chlorococcum humicola, the alga's pyrolytic behavior was studied at heating rates of 5-20K/min in a thermobalance. To model the weight loss characteristics, an algorithm was developed based on the distributed activation energy model and applied to experimental data to extract the kinetics of the decomposition process. When the kinetic parameters estimated by this method were applied to another set of experimental data which were not used to estimate the parameters, the model was capable of predicting the pyrolysis behavior, in the new set of data with a R(2) value of 0.999479. The slow weight loss, that took place at the end of the pyrolysis process, was also accounted for by the proposed algorithm which is capable of predicting the pyrolysis kinetics of C. humicola at different heating rates.
Publisher: Elsevier BV
Date: 2002
Publisher: Springer Science and Business Media LLC
Date: 21-01-2016
Publisher: MDPI AG
Date: 09-02-2022
Abstract: Levoglucosenone (LGO) and 5-chloromethyl furfural (5-CMF) are two bio-based platform chemicals with applications in medicines, green solvents, fuels, and the polymer industry. This study demonstrates the one-step thermochemical conversion of raw and pretreated (delignified) biomass to highly-valuable two platform chemicals in a fluidized bed reactor. Hydrochloric acid gas is utilized to convert biomass thermochemically. The addition of hydrochloric acid gas facilitates the formation of LGO and CMF. Acid gas reacts with biomass to form 5-CMF, which acts as a catalyst to increase the concentration of LGO in the resulting bio-oil. The presence of higher cellulose content in delignified biomass significantly boosts the synthesis of both platform chemicals (LGO and CMF). GC-MS analysis was used to determine the chemical composition of bio-oil produced from thermal and thermochemical conversion of biomass. At 350 °C, the maximum concentration of LGO (27.70 mg/mL of bio-oil) was achieved, whereas at 400 °C, the highest concentration of CMF (19.24 mg/mL of bio-oil) was obtained from hardwood-delignified biomass. The findings suggest that 350 °C is the optimal temperature for producing LGO and 400 °C is optimal for producing CMF from delignified biomass. The secondary cracking process is accelerated by temperatures over 400 °C, resulting in a low concentration of the target platform chemicals. This work reveals the simultaneous generation of LGO and CMF, two high-value commercially relevant biobased compounds.
Publisher: American Chemical Society (ACS)
Date: 13-01-2021
Publisher: American Chemical Society (ACS)
Date: 18-12-2020
Publisher: Elsevier BV
Date: 09-2000
Publisher: Elsevier BV
Date: 07-2018
Publisher: MDPI AG
Date: 21-02-2019
DOI: 10.3390/MA12040655
Abstract: This review focusses on the use of recycled and virgin polymers in mineral and metallurgical processing, both high and ambient temperature processes, including novel applications. End of life applications of polymers as well as the utilisation of polymers during its life time in various applications are explored. The discussion includes applications in cleaner coal production, iron and steel production, iron ore palletisation, iron alloy manufacturing, manganese processing, E-wastes processing and carbon sequestration. The underlying principles of these applications are also explained. Advantages and disadvantages of using these polymers in terms of energy and emission reductions, reduction in non-renewables and dematerialisation are discussed. Influence of the polymers on controlling the evolution of micro and nanostructures in alloys and advanced materials is also considered.
Publisher: Elsevier BV
Date: 04-2020
Publisher: Elsevier BV
Date: 02-2011
Publisher: Elsevier BV
Date: 12-2013
Publisher: Elsevier BV
Date: 08-1999
Publisher: Elsevier BV
Date: 2014
Publisher: American Chemical Society (ACS)
Date: 21-10-2013
DOI: 10.1021/EF401649J
Publisher: American Chemical Society (ACS)
Date: 31-08-2010
DOI: 10.1021/EF100314K
Publisher: Walter de Gruyter GmbH
Date: 15-08-2023
Abstract: Coal and biomass are important feedstocks for carbon energy from thermochemical conversion process. Fully understanding the analytical technology that characterizes the changes in physicochemical properties and structural characteristics of coal and biomass during the thermochemical reactions is a key prerequisite for the realization of appropriate utilization of energy fuels. Modern in-situ process analysis technology can accomplish the in-situ detection of the experimental process, and therefore reflect the experimental process more accurately. Moreover, it is developing towards automation, intelligentization, and comprehensive detection. Based on the characteristics of each detection technology, this paper summarizes the basic principles, application scope and performance characteristics of the three advanced in-situ process analysis technologies: hyphenated technology, synchrotron radiation, and online analysis. The practicability and accuracy of each detection technology in coal and biomass research are compared and analyzed, and its latest application and development trend are elucidated. These tools not only make up for the shortcomings of traditional detection techniques in characterizing the in-situ reaction, but also provide complementary information on molecular microscopic changes during fuel thermal conversion. This review paper can provide insights for relevant researchers in the selection of analytical techniques, and promote in-depth study on microcosmic mechanism of fuel conversion.
Publisher: Hindawi Limited
Date: 25-01-2021
DOI: 10.1002/ER.6475
Publisher: Elsevier BV
Date: 12-2015
Publisher: American Chemical Society (ACS)
Date: 15-02-2012
DOI: 10.1021/EF201694Y
Publisher: Elsevier BV
Date: 05-2005
Publisher: Elsevier BV
Date: 10-2017
Publisher: Elsevier BV
Date: 12-2013
DOI: 10.1016/J.BIORTECH.2013.09.113
Abstract: The combustion characteristics of microalgae, brown coal and their blends under O2/N2 and O2/CO2 atmospheres were studied using thermogravimetry. In microalgae combustion, two peaks at 265 and 485°C were attributable to combustion of protein and carbohydrate with lipid, respectively. The DTG profile of coal showed one peak with maximum mass loss rate at 360°C. Replacement of N2 by CO2 delayed the combustion of coal and microalgae. The increase in O2 concentration did not show any effect on combustion of protein at the first stage of microalgae combustion. However, between 400 and 600°C, with the increase of O2 partial pressure the mass loss rate of microalgae increased and TG and DTG curves of brown coal combustion shifted to lower temperature zone. The lowest and highest activation energy values were obtained for coal and microalgae, respectively. With increased microalgae/coal ratio in the blends, the activation energy increased due to synergy effect.
Publisher: Elsevier BV
Date: 2016
Publisher: Elsevier BV
Date: 12-2018
Publisher: Elsevier BV
Date: 06-2012
Publisher: Elsevier BV
Date: 02-2019
Publisher: Elsevier BV
Date: 1993
Publisher: Springer Berlin Heidelberg
Date: 2013
Publisher: American Chemical Society (ACS)
Date: 26-11-2014
DOI: 10.1021/ES504667R
Abstract: This study investigates, for the first time, the NOx, N2O, SO3, and Hg emissions from combustion of a Victorian brown coal in a 10 kWth fluidized bed unit under oxy-fuel combustion conditions. Compared to air combustion, lower NOx emissions and higher N2O formation were observed in the oxy-fuel atmosphere. These NOx reduction and N2O formations were further enhanced with steam in the combustion environment. The NOx concentration level in the flue gas was within the permissible limit in coal-fired power plants in Victoria. Therefore, an additional NOx removal system will not be required using this coal. In contrast, both SO3 and gaseous mercury concentrations were considerably higher under oxy-fuel combustion compared to that in the air combustion. Around 83% of total gaseous mercury released was Hg(0), with the rest emitted as Hg(2+). Therefore, to control harmful Hg(0), a mercury removal system may need to be considered to avoid corrosion in the boiler and CO2 separation units during the oxy-fuel fluidized-bed combustion using this coal.
Publisher: Elsevier BV
Date: 2014
Publisher: Elsevier BV
Date: 11-2016
Publisher: Elsevier BV
Date: 09-2014
Publisher: American Chemical Society (ACS)
Date: 27-06-2019
Publisher: American Chemical Society (ACS)
Date: 22-10-2012
DOI: 10.1021/IE301530J
Publisher: American Chemical Society (ACS)
Date: 10-04-2014
DOI: 10.1021/EF500306E
Publisher: Elsevier BV
Date: 04-2013
Publisher: Elsevier BV
Date: 08-2016
Publisher: Elsevier BV
Date: 05-2019
DOI: 10.1016/J.WASMAN.2019.03.048
Abstract: Mixed municipal solid waste, consisting of ten major components such as yard waste, food waste, textile, paper, rubber, low-density polyethylene, high-density polyethylene, polypropylene, poly-(ethylene terephthalate) and polystyrene, is studied for performing thermal pyrolysis. Thermogravimetric analysis is utilised to quantify the interactions amongst these components, and also to compute the kinetic parameters of mixed municipal solid waste pyrolysis. The change in kinetic parameters, which is caused by interaction between components, has also been modelled. The calculated ratio of activation energy to the logarithm of the pre-exponential factor (E/logA) predicts the change in stability of the compounds during pyrolysis. For pyrolysis of in idual compounds, the pyrolytic range of compounds is found to be 170-490 °C, with E/logA ranges between 10.54 and 13.9. However, considering all the binary interactions and the complex municipal solid waste matrix, the temperature range of pyrolysis expands to 170-520 °C, with stability ranges varying from 9.98 to 15.32. Furthermore, overlap ratio is calculated to quantify the intensity of these interactions. Rubber is found to cause maximum interactions which impose a negative synergistic effect on the pyrolytic decomposition behaviours of biomass and plastic mixtures, resulting in an overlap ratio of 0.9 and 0.95, respectively, for these mixtures.
Publisher: Elsevier BV
Date: 2014
Publisher: Elsevier BV
Date: 2011
Publisher: Elsevier BV
Date: 04-2011
Publisher: Institute of Electrical and Electronics Engineers (IEEE)
Date: 09-2020
Publisher: Springer Science and Business Media LLC
Date: 18-05-2016
Publisher: Elsevier BV
Date: 09-2017
Publisher: Elsevier BV
Date: 06-2023
Publisher: MDPI AG
Date: 26-07-2021
DOI: 10.3390/EN14154517
Abstract: Reversible solid oxide cells (rSOC) enable the efficient cyclic conversion between electrical and chemical energy in the form of fuels and chemicals, thereby providing a pathway for long-term and high-capacity energy storage. Amongst the different fuels under investigation, hydrogen, methane, and ammonia have gained immense attention as carbon-neutral energy vectors. Here we have compared the energy efficiency and the energy demand of rSOC based on these three fuels. In the fuel cell mode of operation (energy generation), two different routes have been considered for both methane and ammonia Routes 1 and 2 involve internal reforming (in the case of methane) or cracking (in the case of ammonia) and external reforming or cracking, respectively. The use of hydrogen as fuel provides the highest round-trip efficiency (62.1%) followed by methane by Route 1 (43.4%), ammonia by Route 2 (41.1%), methane by Route 2 (40.4%), and ammonia by Route 1 (39.2%). The lower efficiency of internal ammonia cracking as opposed to its external counterpart can be attributed to the insufficient catalytic activity and stability of the state-of-the-art fuel electrode materials, which is a major hindrance to the scale-up of this technology. A preliminary cost estimate showed that the price of hydrogen, methane and ammonia produced in SOEC mode would be ~1.91, 3.63, and 0.48 $/kg, respectively. In SOFC mode, the cost of electricity generation using hydrogen, internally reformed methane, and internally cracked ammonia would be ~52.34, 46.30, and 47.11 $/MWh, respectively.
Publisher: Elsevier BV
Date: 09-2014
Publisher: Elsevier BV
Date: 11-2016
Publisher: Elsevier BV
Date: 2018
Publisher: Elsevier BV
Date: 09-2014
Publisher: Elsevier BV
Date: 04-2017
Publisher: Royal Society of Chemistry (RSC)
Date: 2023
DOI: 10.1039/D3SE00219E
Abstract: The dilemma of fossil fuel use, political versatility, and global climate change have driven motivation that has led to growing interest in developing and implementing renewable energy and green chemical technologies.
Publisher: ASME International
Date: 11-1994
DOI: 10.1115/1.2911447
Publisher: Elsevier BV
Date: 2020
Publisher: Elsevier BV
Date: 10-1996
Publisher: Elsevier BV
Date: 10-2015
Publisher: American Chemical Society (ACS)
Date: 07-06-2012
DOI: 10.1021/EF300559B
Publisher: Royal Society of Chemistry (RSC)
Date: 2021
DOI: 10.1039/D1RE00035G
Abstract: Alkaline slags, a waste product of steel industry, provide an opportunity for carbon sequestration and creation of value at the same time. This requires an understanding of the mechanisms of leaching and carbonation.
Publisher: Elsevier BV
Date: 2014
DOI: 10.1016/J.BIORTECH.2013.10.034
Abstract: Three types of woody biomass were investigated under pyrolysis condition to observe the change in the surface functional groups by Fourier transform infrared (FTIR) technique with increasing temperature under two different (5 and 150°C/min) heating rates. The experiments were carried out in situ in the infrared microscopy beamline (IRM) of the Australian Synchrotron. The capability of the beamline made it possible to focus on single particles to obtain low noise measurements without mixing with KBr. At lower heating rate, the surface functional groups were completely removed by 550°C. In case of higher heating rate, a delay was observed in losing the functional groups. Even at a high temperature, significant number of functional groups was retained after the higher heating rate experiments. This implies that at considerably high heating rates typical of industrial reactors, more functional groups will remain on the surface.
Publisher: Elsevier BV
Date: 05-2014
Publisher: Wiley
Date: 18-02-2016
DOI: 10.1002/AIC.15198
Publisher: Elsevier
Date: 2017
Publisher: Elsevier BV
Date: 09-2016
Publisher: American Chemical Society (ACS)
Date: 28-09-2011
DOI: 10.1021/EF2011595
Publisher: Elsevier BV
Date: 09-2015
Publisher: Elsevier BV
Date: 08-2022
Publisher: Elsevier BV
Date: 09-2015
Publisher: American Chemical Society (ACS)
Date: 06-12-2021
Publisher: Elsevier BV
Date: 11-2016
Publisher: Elsevier BV
Date: 2011
Publisher: Elsevier BV
Date: 02-2020
DOI: 10.1016/J.WASMAN.2019.10.029
Abstract: Catalytic pyrolysis is a useful technique for the conversion of scrap tyres into liquid fuels. Zeolite catalysts were employed in the pyrolysis of scrap tyres for the production of aromatic rich fuel. Deactivation of zeolite catalysts during pyrolysis reaction was investigated which played an important role in the product quality and composition. Herein, the performance of microporous zeolite catalysts and mesoporous MCM-41 catalyst was evaluated in a two-stage fixed bed reactor for the pyrolysis of scrap tyres. Comparative studies showed the increase in the production of aromatic compounds up to 23.7% over zeolite catalyst as compared to 18.7% over MCM-41 catalyst. However, Zeolite Y catalyst exhibited higher coke formation led to the rapid deactivation. The stability of zeolite catalysts is addressed by the incorporation of Cerium metal within the framework of two zeolite catalysts namely Zeolite Y and ZSM-5 through the ion-exchange technique. Parent and spent catalysts were characterised using synchrotron FT-IR spectroscopy, temperature-programmed desorption of ammonia (NH
Publisher: Elsevier BV
Date: 04-2017
DOI: 10.1016/J.BIORTECH.2017.01.005
Abstract: This two-part study firstly investigated Tetraselmis suecica grown in different CO
Publisher: Springer Science and Business Media LLC
Date: 30-09-2015
Publisher: Elsevier BV
Date: 10-2015
Publisher: ASME International
Date: 04-2004
DOI: 10.1115/1.1666885
Abstract: This note presents results of a theoretical and experimental investigation on the emittance of particulate deposits. A simple model based on independent and multiple scattering and using discrete ordinate method has been developed to predict the spectral hemispherical and normal emittance of particulate deposits. The model predictions are compared with measurements carried out under this study-controlled spectral emission measurements between wavelengths of 2 and 12 μm on deposits of ground synthetic ash particles having known composition and particle size. The trends from the predictions matched well with the measured values, except for some differences in the wavelength region below 4 μm, and between 8 μm and 12 μm wavelength. Possible reasons for these differences are discussed.
Publisher: Elsevier BV
Date: 11-2019
Publisher: Royal Society of Chemistry (RSC)
Date: 2022
DOI: 10.1039/D1SE01333E
Abstract: The search for sustainable routes for the production of C 3 chemicals by using renewable feedstocks has attracted significant interest from academic and industrial communities to alleviate the shortage of fossil fuels.
Publisher: American Chemical Society (ACS)
Date: 05-02-2013
DOI: 10.1021/ES303364G
Abstract: Sulfur emission from a Victorian brown coal was quantitatively determined through controlled experiments in a continuously fed drop-tube furnace under three different atmospheres: pyrolysis, oxy-fuel combustion, and carbon dioxide gasification conditions. The species measured were H(2)S, SO(2), COS, CS(2), and more importantly SO(3). The temperature (873-1273 K) and gas environment effects on the sulfur species emission were investigated. The effect of residence time on the emission of those species was also assessed under oxy-fuel condition. The emission of the sulfur species depended on the reaction environment. H(2)S, SO(2), and CS(2) are the major species during pyrolysis, oxy-fuel, and gasification. Up to 10% of coal sulfur was found to be converted to SO(3) under oxy-fuel combustion, whereas SO(3) was undetectable during pyrolysis and gasification. The trend of the experimental results was qualitatively matched by thermodynamic predictions. The residence time had little effect on the release of those species. The release of sulfur oxides, in particular both SO(2) and SO(3), is considerably high during oxy-fuel combustion even though the sulfur content in Morwell coal is only 0.80%. Therefore, for Morwell coal utilization during oxy-fuel combustion, additional sulfur removal, or polishing systems will be required in order to avoid corrosion in the boiler and in the CO(2) separation units of the CO(2) capture systems.
Publisher: Springer Science and Business Media LLC
Date: 10-05-2018
DOI: 10.1038/S41598-018-25787-W
Abstract: Direct C-O hydrogenolysis of bioglycerine to produce 1,3-propanediol selectively is a vital technology that can expand the scope of biodiesel industry and green chemical production from biomass. Herein we report sulphuric acid-activated montmorillonite clay supported platinum nanoparticles as highly effective solid acid catalysts for the selective production of 1,3-propanediol from glycerol. The catalytic performances of the catalysts were investigated in the hydrogenolysis of glycerol with a fixed bed reactor under ambient pressure. The results were found promising and showed that the activation of montmorillonite by sulphuric acid incorporated Brønsted acidity in the catalyst and significantly improved the selectivity to 1,3-propanediol. The catalytic performance of different platinum loaded catalysts was examined and 2 wt% Pt/S-MMT catalyst presented superior activity among others validating 62% 1,3-propanediol selectivity at 94% glycerol conversion. The catalytic activity of 2Pt/S-MMT was systematically investigated under varying reaction parameters including reaction temperature, hydrogen flow rate, glycerol concentration, weight hourly space velocity, and contact time to derive the optimum conditions for the reaction. The catalyst stability, reusability and structure-activity correlation were also elucidated. The high performance of the catalyst could be ascribed to well disperse Pt nanoparticles immobilized on acid-activated montmorillonite, wider pore-structure and appropriate acid sites of the catalyst.
Publisher: MDPI AG
Date: 09-09-2018
DOI: 10.3390/CATAL8090385
Abstract: The catalytic conversion of glycerol to value-added propanols is a promising synthetic route that holds the potential to overcome the glycerol oversupply from the biodiesel industry. In this study, selective hydrogenolysis of 10 wt% aqueous bio-glycerol to 1-propanol and 2-propanol was performed in the vapor phase, fixed-bed reactor by using environmentally friendly bifunctional Pd/MoO3-Al2O3 catalysts prepared by wetness impregnation method. The physicochemical properties of these catalysts were derived from various techniques such as X-ray diffraction, NH3-temperature programmed desorption, scanning electron microscopy, 27Al NMR spectroscopy, surface area analysis, and thermogravimetric analysis. The catalytic activity results depicted that a high catalytic activity ( %) with very high selectivity ( %) to 1-propanol and 2-propanol was obtained over all the catalysts evaluated in a continuously fed, fixed-bed reactor. However, among all others, 2 wt% Pd/MoO3-Al2O3 catalyst was the most active and selective to propanols. The synergic interaction between the palladium and MoO3 on Al2O3 support and high strength weak to moderate acid sites of the catalyst were solely responsible for the high catalytic activity. The maximum glycerol conversion of 88.4% with 91.3% selectivity to propanols was achieved at an optimum reaction condition of 210 ∘ C and 1 bar pressure after 3 h of glycerol hydrogenolysis reaction.
Publisher: Elsevier BV
Date: 09-2019
Publisher: Elsevier BV
Date: 09-2021
Publisher: MDPI AG
Date: 04-09-2023
Publisher: Royal Society of Chemistry (RSC)
Date: 2019
DOI: 10.1039/C8RE00167G
Abstract: Achievement of high calcium carbonate supersaturation without surface passivation is the way for efficient PCC production and CO 2 utilisation using steel slag.
Publisher: Elsevier BV
Date: 11-2015
Publisher: Springer Science and Business Media LLC
Date: 14-07-2015
Publisher: Elsevier BV
Date: 10-2014
Publisher: Elsevier BV
Date: 02-2013
Publisher: Elsevier BV
Date: 09-2017
Publisher: American Chemical Society (ACS)
Date: 31-05-2011
DOI: 10.1021/EF200250C
Publisher: Royal Society of Chemistry (RSC)
Date: 2019
DOI: 10.1039/C8CY02035C
Abstract: Ethylene glycol (EG) is a commodity chemical commercially produced via oxidation of the petrochemical-based resource, ethylene.
Publisher: American Chemical Society (ACS)
Date: 09-04-2015
Publisher: Elsevier BV
Date: 2019
Publisher: Elsevier BV
Date: 09-1995
Publisher: American Chemical Society (ACS)
Date: 08-10-2014
DOI: 10.1021/EF501480G
Publisher: Elsevier BV
Date: 10-2015
Publisher: Wiley
Date: 26-11-2019
DOI: 10.1002/BBB.2066
Publisher: Elsevier BV
Date: 12-1997
Publisher: Elsevier BV
Date: 06-2011
Publisher: Elsevier BV
Date: 02-2016
Start Date: 01-2025
End Date: 01-2029
Amount: $4,955,854.00
Funder: Australian Research Council
View Funded ActivityStart Date: 2018
End Date: 12-2022
Amount: $267,804.00
Funder: Australian Research Council
View Funded ActivityStart Date: 2010
End Date: 12-2012
Amount: $360,000.00
Funder: Australian Research Council
View Funded ActivityStart Date: 02-2007
End Date: 06-2010
Amount: $589,326.00
Funder: Australian Research Council
View Funded ActivityStart Date: 06-2014
End Date: 12-2017
Amount: $1,633,554.00
Funder: Australian Research Council
View Funded ActivityStart Date: 01-2021
End Date: 01-2026
Amount: $3,317,500.00
Funder: Australian Research Council
View Funded ActivityStart Date: 01-2012
End Date: 12-2013
Amount: $300,000.00
Funder: Australian Research Council
View Funded Activity