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Associate Professor Elham Doroodchi

Associate Professor

School of Engineering (Chemical Engineering)

Career Summary

Biography

Dr Doroodchi, an early career researcher, began her PhD studies at the University of Newcastle (UoN) in 2001 after completing her undergraduate studies at the same university with a 1st Class Honours and University Medal, as well as, several other prizes including: the Newcastle University Dean's Medal, 2000, the Institution of Chemical Engineers Prize, 2000, and Deans Merit List, 1998-2000. Dr Doroodchi was awarded an APA Postgraduate Scholarship in 2001 to pursue her doctoral studies. This was followed by a Visiting Postgraduate Fellowship by the Vienna Institute of Technology (Austria) in 2004.

Upon completion of her PhD studies, Dr Doroodchi was awarded a prestigious and competitive Research Fellowship by the UoN. In 2005, the collective efforts of Dr Doroodchi and her colleagues in developing the Reflux Classifier was recognised when Prof Galvin accepted a national award on behalf of the group (National Award, 2005, Business / Higher Education Round Table). The Reflux Classifier since then has been commercialised and marketed to various national and international mineral processing companies.

Although an early career researcher (PhD October 2005), Dr Doroodchi has established a strong track record since joining the Discipline of Chemical Engineering as a Research Fellow. In collaboration with her colleagues in Chemical Engineering, she has been able to secure a total funding of $2,900,000. Also, she has been able to sustain a steady record of quality publications and managed to publish (total of 17 papers) 7 refereed journal, 10 peer reviewed conference papers and 2 patents over the past six years. Apart from her research activities, she has also actively participated in a range of consultancy projects primarily concerned with energy and combustion. Through these, Dr Doroodchi has made significant contribution in solving problems of practical importance to the local industry.

Research Expertise
Dr Doroodchi's research is underpinned by the two general areas of fluid mechanics and particle technology with the main focus being on the fundamental and applied research into multiphase systems. Specifically the research has focused on hydrodynamics of fluidized beds, and solid particle, droplet and bubble motion in fluid. The research carried out by Dr Doroodchi has involved a combination of novel and conventional experimental measurement techniques (e.g. Particle image velocimetry) and theoretical modelling (e.g. Computational fluid dynamics). In all cases, the fundamental understanding of the interaction between the phases is obtained under conditions relevant to the actual industrial-scale and subsequently has been applied to the engineering design of multiphase systems such as particle classifiers, separators and mixers.

Dr Doroodchi has recently applied her knowledge in the fields of multiphase flows and particle technology into the emerging field of microfluidics which has numerous novel applications in medicine, engineering and life sciences. The studies include processing of nano-particles in microdevices, emulsification process in micro-reactors and mixing in micro-channels. The focus is on developing techniques to enhance phase interactions at micro-sized channels. Dr Doroodchis contribution to fluid mechanics of energy systems has led to the development of a novel power cycle for generation of electricity from geothermal resources and the use of waste heat for desalination of brackish water.

Teaching Expertise
Dr Doroodchi has voluntarily contributed to the teaching activities of Chemical Engineering Discipline.

Administrative Expertise
Dr Doroodchi has been recognised as a an expert of international standing by the Australian Research Council (ARC) College of Experts and hence asesses a number of Discovery Projects scheme proposals each year.

Qualifications

  • PhD, University of Newcastle
  • Bachelor of Engineering (Chemical Engineering), University of Newcastle

Keywords

  • Design
  • Fluid Mechanics
  • Heat and Mass Balance
  • Multiphase Flows
  • Particle Technology

Fields of Research

Code Description Percentage
091499 Resources Engineering and Extractive Metallurgy not elsewhere classified 35
130299 Curriculum and Pedagogy not elsewhere classified 5
090499 Chemical Engineering not elsewhere classified 60

Professional Experience

UON Appointment

Title Organisation / Department
Associate Professor University of Newcastle
School of Engineering
Australia

Academic appointment

Dates Title Organisation / Department
26/06/2015 - 26/07/2015 ARC IntReader ARC (Australian Research Council)
Australia
1/06/2007 - 1/01/2013 Fellow UON

UoN Research Fellowship

University of Newcastle
School of Engineering
Australia

Membership

Dates Title Organisation / Department
Member - Institution of Engineers, Australia Institution of Engineers, Australia (IEAus)
Australia
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Publications

For publications that are currently unpublished or in-press, details are shown in italics.


Journal article (61 outputs)

Year Citation Altmetrics Link
2016 Yin F, Shah K, Zhou C, Tremain P, Yu J, Doroodchi E, Moghtaderi B, 'Novel Calcium-Looping-Based Biomass-Integrated Gasification Combined Cycle: Thermodynamic Modeling and Experimental Study', Energy and Fuels, 30 1730-1740 (2016)

© 2015 American Chemical Society.The current work focuses on the development of a novel calcium-looping-based biomass-integrated gasification combined cycle (CL-BIGCC) process. T... [more]

© 2015 American Chemical Society.The current work focuses on the development of a novel calcium-looping-based biomass-integrated gasification combined cycle (CL-BIGCC) process. The process is expected to improve the energy density of synthesis gas by capturing CO2 in a carbonator. Also, at the same time, the carbonator is expected to act as an ex situ tar removal unit, where tar cracking is expected to occur via catalytic reactions with CaO. The current work evaluates the feasibility of the proposed CL-BIGCC concept via thermodynamic analysis using Aspen Plus. Moreover, the tar cracking ability of CaO is demonstrated using thermogravimetric analyzer coupled to Fourier transform infrared spectrometer (TGA-FTIR) experiments. As part of the thermodynamic analysis, sensitivity analyses of the key process parameters, such as the calcium/biomass (Ca/B) ratio, steam/biomass (S/B) ratio, carbonator temperature, and calciner temperature, and their effects on net thermal-to-electricity efficiency have been studied in detail. The optimal values of key process parameters, such as a compression ratio of 5.1, an air/fuel mass ratio of 15, a Ca/B ratio of 0.53, a S/B ratio of 0.17, and carbonator and calciner temperatures of 650 and 800 °C, respectively, have been obtained. Furthermore, the CL-BIGCC process simulated in the current work was found to have a net thermal-to-electricity efficiency of ~25% based on the above optimal parameters, which is the highest among other conventional steam-based BIGCC processes. The biomass gasification (i.e., partial oxidation) experiments in a TGA-FTIR with a CaO/biomass ratio of 1:1 at different temperatures showed that CaO effectively catalyzed tar-cracking reactions.

DOI 10.1021/acs.energyfuels.5b02266
Co-authors Kalpit Shah, Behdad Moghtaderi
2016 Zhou C, Shah K, Song H, Zanganeh J, Doroodchi E, Moghtaderi B, 'Integration Options and Economic Analysis of an Integrated Chemical Looping Air Separation Process for Oxy-fuel Combustion', Energy and Fuels, 30 1741-1755 (2016)

© 2015 American Chemical Society.This paper is concerned about a detailed techno-economic assessment of a hypothetical 500 MWe coal-fired power plant in New South Wales, Australi... [more]

© 2015 American Chemical Society.This paper is concerned about a detailed techno-economic assessment of a hypothetical 500 MWe 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).

DOI 10.1021/acs.energyfuels.5b02209
Co-authors Behdad Moghtaderi, Kalpit Shah
2016 Galvin KP, Forghani M, Doroodchi E, Iveson SM, 'Consolidation of non-colloidal spherical particles at low particle Reynolds numbers', KONA Powder and Particle Journal, 2016 249-263 (2016)

© 2016 Hosokawa Powder Technology Foundation.When a system of identical spheres settles under conditions of negligible surface and inertial forces an idealised form of sediment c... [more]

© 2016 Hosokawa Powder Technology Foundation.When a system of identical spheres settles under conditions of negligible surface and inertial forces an idealised form of sediment consolidation unfolds amenable to a universal description. We have described this complex process using a simple constitutive model expressed as an elementary scaling law in time, t, applied at the local particle level. The free-volume surrounding a particle consists of two volume contributions occupied by fluid, one portion fixed and the other portion variable, the latter of which declines with t¿2 . A comprehensive system of analytical equations was derived using this one idea, and associated boundary conditions, to describe all aspects of the batch settling process. An experimental system exhibiting negligible surface and inertial forces was used to validate the model and hence assess the merits of the scaling law. Excellent agreement was achieved. The precise physics responsible for this scaling law, and the applicable boundary conditions, remain unclear at this stage. Hence this work is likely to motivate further work in this area, concerned with the dynamics of random consolidation of settling spheres.

DOI 10.14356/kona.2016006
Co-authors Kevin Galvin
2016 Khairul MA, Shah K, Doroodchi E, Azizian R, Moghtaderi B, 'Effects of surfactant on stability and thermo-physical properties of metal oxide nanofluids', International Journal of Heat and Mass Transfer, 98 778-787 (2016)

© 2016 Elsevier Ltd. All rights reserved.Optimal thermo-physical properties of nanofluids provide an opportunity to overcome energy associated difficulties, in addition to provid... [more]

© 2016 Elsevier Ltd. All rights reserved.Optimal thermo-physical properties of nanofluids provide an opportunity to overcome energy associated difficulties, in addition to providing new alternatives to catch, store and exchange of energy. A significant reduction in energy consumption is possible by improving the performance of a heat exchanger circuit, and may in part alleviate current energy related challenging issues such as global warming, climate change, and the fuel crisis. The objective of this work is to gain an insight into the overall stability of nanofluids with respect to pH, zeta potential, particle size distribution, and its effect on viscosity and thermal conductivity. For the purpose of this study two nanofluids were selected (water based alumina and copper oxide). Various nanoparticles concentrations as well as anionic surfactants (sodium dodecylbenzene sulfonate) were investigated for their stability, viscosity as well as thermal conductivity. The results clearly showed that nanofluid stability has a strong relation with viscosity and thermal conductivity. The stability of the nanofluid was found to be improved with a decrease in viscosity and an increase in thermal conductivity.

DOI 10.1016/j.ijheatmasstransfer.2016.03.079
Co-authors Behdad Moghtaderi, Mohammadkhairul Alam Uon
2016 Mitra S, Nguyen TBT, Doroodchi E, Pareek V, Joshi JB, Evans GM, 'On wetting characteristics of droplet on a spherical particle in film boiling regime', Chemical Engineering Science, 149 181-203 (2016)

© 2016.This study reports droplet-particle interaction of size ratio less than unity in the film boiling regime on a highly thermally conductive spherical particle surface. Speci... [more]

© 2016.This study reports droplet-particle interaction of size ratio less than unity in the film boiling regime on a highly thermally conductive spherical particle surface. Specifically, the effects of impact Weber number (We) of subcooled state droplets comprising water (We=3.9-103.6) and isopropyl alcohol (IPA) (We=8.6-194.6) were studied using high speed imaging technique in the particle temperature range of 250-350 °C. In general, non-wetting interaction behaviour was observed with two distinct outcomes - rebound and complete disintegration demarcated by a critical Weber number range instead of a single threshold value. Extent of surface wetting was characterised by the maximum droplet spread diameter parameter which was found to scale with impact Weber number in a power law form which agrees with the theoretical scaling argument. Additionally, an energy balance model was developed to compute this parameter which provided good agreement with the experimental measurements in the lower Weber number regime, however, higher deviations were noted near the transition regime. Also quantified from experiments was the droplet-particle contact time which exhibited a power law dependency on Weber number in the rebound regime, however, was noted to be almost independent of Weber number in the disintegration regime. Particle surface wettability was characterised by the experimentally measured dynamic contact angles which were found to vary in the range of 120-160o in low Weber number regime manifesting the hydrophobic nature of particle surface in film boiling regime. Also, all the parameters such as contact line velocity, particle temperature and droplet size apparently had relatively insignificant influence on the variation of dynamic contact angle. Temporal variation of non-dimensional spreading parameter exhibited a self-similar behaviour wherein all data collapsed on a single power law profile. It was further shown that the behaviour could also be described by a recovery type exponential profile through suitable non-dimensionalization and both profiles can be utilized to produce a spreading kinetics.

DOI 10.1016/j.ces.2016.04.003
Co-authors Geoffrey Evans, Subhasish Mitra
2016 Alghamdi Y, Peng Z, shah K, Moghtaderi B, Doroodchi E, 'A correlation for predicting solids holdup in the dilute pneumatic conveying flow regime of circulating and interconnected fluidised beds', Powder Technology, 297 357-366 (2016)

© 2016 Elsevier B.V.Theoretical modelling, design and operation of circulating and interconnected fluidized beds require an accurate prediction of solids holdup in the fully deve... [more]

© 2016 Elsevier B.V.Theoretical modelling, design and operation of circulating and interconnected fluidized beds require an accurate prediction of solids holdup in the fully developed pneumatic conveying flow regime of the riser (i.e. the upper section of the riser). Existing empirical and semi-empirical solids holdup correlations have exhibited limited accuracy and application range. In this study, an empirical correlation was developed to predict the solids holdup at the upper section of the riser in circulating and interconnected fluidized beds with an improved level of accuracy for a broad range of operating conditions and riser dimensions. The correlation is based on a group of dimensionless quantities, which are typically used to describe the hydrodynamics of gas-solids fluidized beds, taking into account gas and particle properties, riser dimensions, and solid circulation rate. The reduced solids flux phenomenon also has been considered directly by introducing a system dependent exponent in the correlation. The correlation predicted 90% of the experimental data with an average deviation of 15%. The correlation is applicable for particle Reynolds numbers between 3.7 and 366.

DOI 10.1016/j.powtec.2016.04.037
Co-authors Behdad Moghtaderi
2016 Peng Z, Joshi JB, Moghtaderi B, Khan MS, Evans GM, Doroodchi E, 'Segregation and dispersion of binary solids in liquid fluidised beds: A CFD-DEM study', Chemical Engineering Science, 152 65-83 (2016)

© 2016 Elsevier Ltd.Liquid fluidised beds often operate with particles of different sizes and densities, encountering partial or complete segregation of solid particles at certai... [more]

© 2016 Elsevier Ltd.Liquid fluidised beds often operate with particles of different sizes and densities, encountering partial or complete segregation of solid particles at certain operating conditions. In this study, the segregation and dispersion of binary particle species of the same size but different densities in liquid fluidised beds have been investigated based on the analysis of computational fluid dynamics - discrete element method (CFD-DEM) simulation results.The vertical fluid drag force acting on the particles was found to be responsible for the particle segregation. The mechanisms governing the particle dispersion strongly depended upon the solid-liquid two-phase flow regime, which transited from pseudo-homogeneous to heterogeneous when the superficial liquid velocity reached a certain value. In the homogeneous or pseudo-homogeneous flow regime (Rep=40, ¿L, ave=0.74), particle collisions acted as the main mechanism that drove the dispersion of particles. However, after the system became heterogeneous, the magnitude of the vertical collision force decreased towards zero and correspondingly, the magnitude of the vertical fluid drag force was approaching that of the particle net weight force as the superficial liquid velocity increased. Therefore, in the heterogeneous flow regime (Rep>40, ¿L, ave>0.74), the local turbulence of the fluid flow and particle collisions (if there were any) were found to be the main mechanisms that drove the dispersion of particles in all directions. The dispersion coefficient of individual particles varied significantly throughout the system in the heterogeneous flow regime. The simulation results reasonably agreed with the experimental data and the prediction results by existing correlations.

DOI 10.1016/j.ces.2016.05.032
Citations Scopus - 1
Co-authors Behdad Moghtaderi, Mdshakhaoath Khan Uon, Geoffrey Evans
2016 Azizian R, Doroodchi E, Moghtaderi B, 'Influence of controlled aggregation on thermal conductivity of nanofluids', Journal of Heat Transfer, 138 (2016)

© 2016 by ASME.Nanoparticles aggregation is considered, by the heat transfer community, as one of the main factors responsible for the observed enhancement in the thermal conduct... [more]

© 2016 by ASME.Nanoparticles aggregation is considered, by the heat transfer community, as one of the main factors responsible for the observed enhancement in the thermal conductivity of nanofluids. To gain a better insight into the veracity of this claim, we experimentally investigated the influence of nanoparticles aggregation induced by changing the pH value or imposing a magnetic field on the thermal conductivity of water-based nanofluids. The results showed that the enhancement in thermal conductivity of TiO2-water nanofluid, due to pH-induced aggregation of TiO2 nanoparticles, fell within the ±10% of the mixture theory, while applying an external magnetic force on Fe3O4-water nanofluid led to thermal conductivity enhancements of up to 167%. It is believed that the observed low enhancement in thermal conductivity of TiO2-water nanofluid is because, near the isoelectric point (IEP), the nanoparticles could settle out of the suspension in the form of large aggregates making the suspension rather unstable. The magnetic field however could provide a finer control over the aggregate size and growth direction without compromising the stability of the nanofluid, and hence significantly enhancing the thermal conductivity of the nanofluid.

DOI 10.1115/1.4031730
Citations Scopus - 1Web of Science - 1
Co-authors Behdad Moghtaderi
2016 Gai S, Yu J, Yu H, Eagle J, Zhao H, Lucas J, et al., 'Process simulation of a near-zero-carbon-emission power plant using CO2 as the renewable energy storage medium', International Journal of Greenhouse Gas Control, 47 240-249 (2016)

© 2016 Elsevier Ltd.In this paper, process simulation of a near-zero-carbon-emission power plant using CO2 as the renewable energy storage medium was carried out. Liquid fuels th... [more]

© 2016 Elsevier Ltd.In this paper, process simulation of a near-zero-carbon-emission power plant using CO2 as the renewable energy storage medium was carried out. Liquid fuels that can be burned either in boilers or compression ignition engines to generate electricity have been the target products. The CO2 and H2O produced from combustion are recirculated back to the synthesis units, thus forming a closed cycle of "renewable energy (unstable energy supply) + CO2 + H2O ¿ liquid fuels ¿ electricity (stable supply)". This novel closed loop energy storage process integrated with a 670 MW supercritical power plant was analyzed using the Aspen Plus software package. Methanol was selected as the targeted liquid fuel through three major synthesis routes: CO + H2, CO2 + H2 and CO2 + H2O, in which CO and H2 came from the electrolysis of CO2 and H2O. The performances of the three methanol synthesis routes were thermodynamically analyzed. The results show that the optimal methanol synthesis route is the direct conversion of CO2 and H2O through electrocatalysis when CO2 conversion is above 42%, while when CO2 conversion is below 42% the best choice turned out to be the CO hydrogenation. The direct conversion of (CO2 + H2O) using electrocatalysis method was adopted as the liquid fuel synthesis route for the near-zero-carbon-emission power plant. The overall CO2 emission from the near-zero-carbon-emission power plant is 44.13 kg/MWh accounting for just 6.45% of the advanced coal fired power plant.

DOI 10.1016/j.ijggc.2016.02.001
Citations Scopus - 1
Co-authors Behdad Moghtaderi, Jianglong Yu, John Lucas
2016 Mitra S, Doroodchi E, Evans GM, Pareek V, Joshi JB, 'Interaction dynamics of a spherical particle with a suspended liquid film', AIChE Journal, 62 295-314 (2016)

© 2016 American Institute of Chemical Engineers.Hydrodynamics of collision interactions between a particle and gas-liquid interface such as droplet/film is of keen interest in ma... [more]

© 2016 American Institute of Chemical Engineers.Hydrodynamics of collision interactions between a particle and gas-liquid interface such as droplet/film is of keen interest in many engineering applications. The collision interaction between a suspended liquid (water) film of thickness 3.41±0.04 mm and an impacting hydrophilic particle (glass ballotini) of different diameters (1.1-3.0 mm) in low particle impact Weber number (We=¿lvp2dp/s) range (1.4-33) is reported. Two distinct outcomes were observed-particle retention in the film at lower Weber number and complete penetration of the film toward higher Weber number cases. A collision parameter was defined based on energy balance approach to demarcate these two interaction regimes which agreed reasonably well with the experimental outcomes. It was shown that the liquid ligament forming in the complete penetration cases breaks up purely by "dripping/end pinch-off" mechanism and not due to capillary wave instability. An analytical model based on energy balance approach was proposed to determine the liquid mass entrainment associated with the ligament which compared well with the experimental measurements. A good correlation between the %film mass entrained and the particle Bond number (Bo=¿lgdp2/s) was obtained which indicated a dependency of Bo1.72. Computationally, a three-dimensional CFD model was developed to simulate these interactions using different contact angle boundary conditions which in general showed reasonable agreement with experiment but also indicated deficiency of a constant contact angle value to depict the interaction physics in entirety. The computed force profiles from computational fluid dynamics (CFD) model suggest dominance of the pressure force over the viscous force almost by an order of magnitude in all the Weber number cases studied.

DOI 10.1002/aic.15027
Co-authors Subhasish Mitra, Geoffrey Evans
2016 Zhang Y, Doroodchi E, Moghtaderi B, Han X, Liu Y, 'Hydrogen Production from Ventilation Air Methane in a Dual-Loop Chemical Looping Process', Energy and Fuels, 30 4372-4380 (2016)

© 2016 American Chemical Society.A dual-loop chemical looping process is proposed to produce hydrogen from ventilation air methane (VAM). It mainly consists of two loops, an oxyg... [more]

© 2016 American Chemical Society.A dual-loop chemical looping process is proposed to produce hydrogen from ventilation air methane (VAM). It mainly consists of two loops, an oxygen removal loop and a hydrogen production loop. The oxygen removal loop is a Cu-based chemical looping air separation process, in which the oxygen content is separated through the reversible reaction 4CuO 2Cu2O + O2 + 263.2 kJ/mol.The oxygen-depleted stream is subsequently fed into the hydrogen production loop, where the ultra-low-concentration methane is reformed into highly pure hydrogen. In light of the thermodynamics and experimental results, the oxygen removal temperature should be in the range of 300-400 °C in order to commence the oxidation of Cu2O at a proper kinetics rate while the catalytic combustion of VAM and reduction of copper oxides with methane are inhibited. Two configurations are proposed, and the thermodynamic performance is evaluated by a case study with methane concentration of 0.5 vol%. It was found that the proposed system was able to produce high-purity hydrogen from VAM, and the hydrogen efficiency was as high as 40.4%. If pure O2 is considered as a byproduct, the energy demand was 0.32 kWh/m3 O2, which is significantly lower than the energy demand of conventional cryogenic systems. In addition, a parametric study was conducted to determine the effect of the varying operational parameters, and hence the most suitable values for the parameters are given.

DOI 10.1021/acs.energyfuels.6b00134
Co-authors Behdad Moghtaderi
2016 Peng Z, Moghtaderi B, Doroodchi E, 'A modified direct method for void fraction calculation in CFD-DEM simulations', Advanced Powder Technology, 27 19-32 (2016) [C1]

© 2015 The Society of Powder Technology Japan.The void fraction of computational cells in numerical simulations of particulate flows using computational fluid dynamics-discrete e... [more]

© 2015 The Society of Powder Technology Japan.The void fraction of computational cells in numerical simulations of particulate flows using computational fluid dynamics-discrete element method (CFD-DEM) is often directly (or crudely) calculated assuming that the entire body of a particle lies in the cell at which the particle centroid resides. This direct method is most inexpensive but inaccurate and may lead to simulation instabilities. In this study, a modified version of the direct method has been proposed. In this method, referred to as the particle meshing method (PMM), the particle is meshed and the solid volume in a fluid cell is calculated by adding up the particle mesh volume with the basic working principle being the same as that of the direct method. As a result, the PMM inherits the simplicity and hence the computational advantage from the direct method, whilst allowing for duplicating the particle shape and accurate accounting of particle volume in each fluid cell. The numerical simulation characteristics of PMM including numerical stability, minimum particle grid number, prediction accuracy, and computational efficiency have been examined. The results showed that for a specific cell-to-particle size ratio, there was a minimum particle grid number required to reach the stable simulation. A formula of estimating the minimum particle grid number was derived and discussed. Typically, a particle grid number of about 5 times the minimum number was suggested to achieve the best computational efficiency, which was comparable or even higher than that of simulations using the analytical approach. PMM also exhibited the potential to be applied for complex computational domain geometries and irregular shaped particles.

DOI 10.1016/j.apt.2015.10.021
Citations Scopus - 1
Co-authors Behdad Moghtaderi
2015 Zhou C, Shah K, Doroodchi E, Moghtaderi B, 'Equilibrium thermodynamic analyses of methanol production via a novel Chemical Looping Carbon Arrestor process', Energy Conversion and Management, 96 392-402 (2015) [C1]

© 2015 Elsevier B.V. All rights reserved.Abstract Methanol economy is considered as an alternative to hydrogen economy due to the better handling and storage characteristics of m... [more]

© 2015 Elsevier B.V. All rights reserved.Abstract Methanol economy is considered as an alternative to hydrogen economy due to the better handling and storage characteristics of methanol fuel than liquid hydrogen. This paper is concerned about a comprehensive equilibrium thermodynamic analysis carried out on methanol production via an innovative Chemical Looping Carbon Arrestor/Reforming process being developed at the University of Newcastle in order to reduce both energy consumption and carbon emissions. The detailed simulation revealed thermodynamic limitations within the Chemical Looping Carbon Reforming process however on the other hand it also confirmed that the new concept is a low energy requirement and low emission option compared to other methanol production technologies. Specifically, the mass and energy balance study showed that the Chemical Looping Carbon Reforming process typically consumes approximately 0.76-0.77 mole methane, 0.25-0.27 mole carbon dioxide, 0.49-0.50 mole water, and 0.51 mole iron oxide (in a chemical looping manner) per mole of methanol production. Moreover, the energy efficiency of Chemical Looping Carbon Reforming process was found to be ~64-70% and its emission profile was found as low as 0.14 mole carbon dioxide per mole of methanol, which is about 82-88% less than the conventional methanol production process and well below the emission levels of other emerging methanol production technologies.

DOI 10.1016/j.enconman.2015.03.008
Citations Scopus - 3Web of Science - 3
Co-authors Behdad Moghtaderi, Kalpit Shah
2015 Shah K, Zhou C, Song H, Doroodchi E, Moghtaderi B, 'A novel hybrid chemical-looping oxy combustor process for the combustion of solid and gaseous fuels: Thermodynamic analysis', Energy and Fuels, 29 602-617 (2015) [C1]

© 2014 American Chemical Society.The larger reactor volume, additional oxygen polishing unit, and carbon stripper for the separation of oxygen carriers and ash in the chemical lo... [more]

© 2014 American Chemical Society.The larger reactor volume, additional oxygen polishing unit, and carbon stripper for the separation of oxygen carriers and ash in the chemical looping combustion (CLC) and/or chemical looping oxygen uncoupling (CLOU) processes for solid fuels are anticipated not only to incur operational complexity but also to increase the capital and operating costs. As an alternative, this paper proposes a novel hybrid process, called "Chemical Looping Oxy Combustor (CLOC)". This novel process provides an integration of chemical looping air separation (CLAS) with fluidized bed oxy-fuel combustion and is expected to eliminate the need for an additional oxygen polishing unit and carbon stripper. It can be retrofitted to any existing coal circulating fluidized bed (CFB) at low cost. The other advantages of CLOC includes less solid handling issues, flexibility in handling low-grade coal with high moisture, no/less contamination of oxygen carriers, no/less slip of CO2/SOx in an air reactor, low energy penalty, etc. Also, in the CLOC process, coal combustion will occur in a separate fluidized bed combustor with relatively faster kinetics, because of the availability of high oxygen concentration (i.e., ~25-28 vol-"%), which eliminates the need for a larger fuel reactor volume. In the current paper, thermodynamic simulations of CLOC process using Cu-, Mn-, and Co-based metal oxide oxygen carriers were performed. Their performances were also compared against the conventional air-firing and oxy-firing technologies, e.g., oxy-fuel combustion integrated with cryogenic air separation unit (CASU) and CLOU. It was identified that the CLOC process needs external heat for reduction reactor provided by either direct or indirect methane combustion. Moreover, a maximum plant thermal efficiency was achieved for CLOC using Cu-based oxygen carrier. The energy penalty of the CLOC process, compared with the air-firing base case, was found to be ~2%-3%, which is ~4-5 times smaller than those of the CASU cases and only half of that of the CLOU process, indicating that CLOC offers a promising option for the combustion of solid fuels.

DOI 10.1021/ef502389t
Citations Scopus - 3Web of Science - 2
Co-authors Kalpit Shah, Behdad Moghtaderi
2015 Zhang Y, Doroodchi E, Moghtaderi B, 'Reduction kinetics of Fe2O3/Al2O3 by ultralow concentration methane under conditions pertinent to chemical looping combustion', Energy and Fuels, 29 337-345 (2015) [C1]

© 2014 American Chemical Society.Fe2O3/Al2O3 is found to be a suitable oxygen carrier candidate for the chemical looping combustion with ultralow methane concentration in a previ... [more]

© 2014 American Chemical Society.Fe2O3/Al2O3 is found to be a suitable oxygen carrier candidate for the chemical looping combustion with ultralow methane concentration in a previous study by our team. In order to facilitate the fundamental reactor design and understand the energy consumption, the reduction kinetics mechanism of Fe2O3 (hematite) with 0.5 vol % CH4 was determined and the kinetic parameters were estimated based on the thermogravimetric analysis. Two oxygen carriers (i.e., Fe25Al and Fe45Al) were prepared and used in the TGA experiment. It was observed that the reduction of Fe2O3 was a two-steps process. Initially, Fe2O3 is transformed into Fe3O4 (magnetite) at a fast reaction rate and followed by a slow step corresponding to the reduction from Fe3O4 to FeAl2O4. A topochemical approach associated with Hancock and Sharp's method was therefore applied to determine the most suitable kinetic model for the reduction process. It was found that the initial fast step can be described by the Avrami-Erofe'ev phase change model, the A2 model for low conversion, and the A3 model for high conversion, whereas the reaction for the second step was in diffusion control. It also can be concluded that within the Fe2O3 content of 25-45 wt %, there is no difference on the reduction kinetic mechanism and similar activation energy was obtained, which can be comparable with the findings in the literature.

DOI 10.1021/ef5024252
Citations Scopus - 4Web of Science - 4
Co-authors Behdad Moghtaderi
2015 Zhang Y, Doroodchi E, Moghtaderi B, 'Comprehensive study of Fe2O3/Al2O3 reduction with ultralow concentration methane under conditions pertinent to chemical looping combustion', Energy and Fuels, 29 1951-1960 (2015) [C1]

© 2015 American Chemical Society.An experimental study was conducted to identify the most suitable alumina-supported iron-based oxygen carrier for the abatement of ultralow conce... [more]

© 2015 American Chemical Society.An experimental study was conducted to identify the most suitable alumina-supported iron-based oxygen carrier for the abatement of ultralow concentration methane using a chemical looping approach. This was done by evaluating the performance characteristics such as reactivity, cyclic stability, and gas conversion. The experiments were carried out in a thermogravimetric analyzer and a fixed bed reactor setup under the desired conditions. Thermodynamics analysis was carried out using the commercially available software ASPENPLUS. The analysis suggested that the favorable iron-based oxygen carriers were those with the weight content of Fe2O3 less than 50 wt %. Three Fe2O3/Al2O3 samples were therefore prepared with the metal oxide contents in the range of 10-45 wt %, i.e., Fe10Al, Fe25Al, and Fe45Al. The thermogravimetric analysis experimental results showed that the reduction reactivity and stability were improved with the addition of support material compared with unsupported Fe2O3. Moreover, the reduction reactivity varied with the solid conversion range and the weight content of the parent material. For full reduction of Fe2O3 to Fe3O4, the sample Fe10Al showed the highest reduction reactivity. However, in terms of the rate of oxygen transport (which considers the combined effects of the oxygen transfer capacity and reactivity), the highest value was achieved by the Fe45Al sample. The gas conversion of CH4 to CO2 was also quite dependent on the weight content of Fe2O3. Essentially, Fe45Al delivered the longest duration on high-level conversion (i.e., complete conversion of CH4 to CO2). In summary, Fe45Al was found to be the most suitable oxygen carrier candidate in this application. The effect of operational parameters was further examined with various reaction temperatures (873-1073 K), methane concentrations (0.1-1.5 vol %), and CO2 compositions (0-50 vol %).

DOI 10.1021/acs.energyfuels.5b00080
Citations Scopus - 1Web of Science - 1
Co-authors Behdad Moghtaderi
2015 Zhou C, Tremain P, Doroodchi E, Moghtaderi B, Shah K, 'A novel slag carbon arrestor process for energy recovery in steelmaking industry', Fuel Processing Technology, (2015)

© 2015.A novel slag carbon arrestor process (SCAP) was proposed to improve the heat recovery in energy-intensive steelmaking process, which typically has a low heat recovery. The... [more]

© 2015.A novel slag carbon arrestor process (SCAP) was proposed to improve the heat recovery in energy-intensive steelmaking process, which typically has a low heat recovery. The proposed SCAP process introduces a tar reformer to utilise the slag - a by-product from steelmaking process - as the catalyst to convert coke oven gas and tar into hydrogen-enriched fuel gas. This is achieved by making use of the valuable carbon and/or energy contained in the coke oven gas, which otherwise being wasted, to assist in tar reforming and produce hydrogen-enriched gas. Such concept is expected to reduce the undesired tar formation in steelmaking process along with improved heat recovery efficiency and higher quality coke oven gas production. Both simulation and experimental studies on the slag carbon arrestor process were performed. The preliminary thermodynamic analysis carried out using Aspen Plus v8.4 indicates that with the tar reformer the energy content of coke oven gas was found increased from ~34.6MJ/kg to ~37.7MJ/kg (or by 9%). Also, with the utilisation of carbon deposition on the slag, a reduction of up to 12.8% coke usage in the steelmaking process can be achieved. This corresponds to an energy saving of 4% and a carbon emission reduction of 5.7% compared with the conventional steelmaking process. Preliminary experimental TGA-FTIR investigations revealed a reduction in the aromatic and aliphatic hydrocarbon groups and an increase in the production of CO2 and CO, attributed to the tar cracking abilities of slag.

DOI 10.1016/j.fuproc.2016.05.006
Co-authors Kalpit Shah, Behdad Moghtaderi
2015 Shah K, Moghtaderi B, Doroodchi E, Sandford J, 'A feasibility study on a novel stone dust looping process for abatement of ventilation air methane', Fuel Processing Technology, 140 285-296 (2015) [C1]

© 2015 Elsevier Ltd. All rights reserved.This paper describes the development of a novel stone dust looping process that relates to the removal of ventilation air methane using s... [more]

© 2015 Elsevier Ltd. All rights reserved.This paper describes the development of a novel stone dust looping process that relates to the removal of ventilation air methane using stone dust. The working principle behind the stone dust looping process is incredibly simple which involves the catalytic oxidation of methane followed by carbonation and calcination reactions. In the current work, laboratory scale fluidized bed experiments and process simulations were conducted to evaluate the feasibility of the stone dust looping process. The experimental work concluded that oxidation of ventilation air methane in the stone dust looping process can be successfully achieved at temperatures between 500 and 650 °C. The experimental results indicated that oxidation of methane was found to increase at higher temperatures while carbon dioxide capture efficiency showed a declining trend with increasing temperature. Furthermore, higher methane conversion and optimum (thermodynamic) carbon dioxide capture efficiency were observed for lower ventilation air methane flow rates and higher bed inventory. The concentration of methane in ventilation air methane and stone dust particle size did not have a significant effect on methane conversion or carbon dioxide capture. Also, comparison with synthetically prepared CuO and Fe2O3 catalysts has been made with CaO for VAM oxidation. CaO was found to be comparable to Fe2O3 and superior to CuO. From the process simulations, it was concluded that thermal energy generation in the carbonator was increased with higher methane and carbon dioxide concentrations. However, at the same time for higher methane and carbon dioxide concentrations, a greater CaO flux was required in the carbonator and hence a larger amount of goaf gas was required for the calcination reaction. The higher thermal energy generation in the carbonator was expected to improve the autothermicity of the stone dust looping process at concentrations of methane in the ventilation stream < 0.2 vol.% (thermodynamic limit).

DOI 10.1016/j.fuproc.2015.07.031
Citations Scopus - 3Web of Science - 2
Co-authors Behdad Moghtaderi, Kalpit Shah
2015 Ramezani M, Shah K, Doroodchi E, Moghtaderi B, 'Application of a novel calcium looping process for production of heat and carbon dioxide enrichment of greenhouses', Energy Conversion and Management, 103 129-138 (2015) [C1]

© 2015 Elsevier Ltd.Abstract Greenhouses typically employ conventional burner systems to suffice heat and carbon dioxide required for plant growth. The energy requirement and car... [more]

© 2015 Elsevier Ltd.Abstract Greenhouses typically employ conventional burner systems to suffice heat and carbon dioxide required for plant growth. The energy requirement and carbon dioxide emissions from fossil fuel burner are generally high. As an alternative, this paper describes a novel greenhouse calcium looping process which is expected to decrease the energy requirements and associated carbon dioxide emissions. The conceptual design of greenhouse calcium looping process is carried out in the ASPEN Plus v 7.3 simulator. In a greenhouse calcium looping process, the calcination reaction is considered to take place during day time in order to provide the required optimum carbon dioxide between 1000 and 2000 ppm, while the carbonation reaction is occurred during night time to provide required heat. The process simulations carried out in ASPEN indicates that greenhouse calcium looping process theoretically attributes to zero emission of carbon dioxide. Moreover, in a scenario modelling study compared to the conventional natural gas burner system, the heat duty requirements in the greenhouse calcium looping process were found to reduce by as high as 72%.

DOI 10.1016/j.enconman.2015.06.044
Citations Scopus - 3Web of Science - 2
Co-authors Behdad Moghtaderi, Kalpit Shah
2015 Peng Z, Doroodchi E, Alghamdi YA, Shah K, Luo C, Moghtaderi B, 'CFD-DEM simulation of solid circulation rate in the cold flow model of chemical looping systems', Chemical Engineering Research and Design, 95 262-280 (2015) [C1]

© 2014 The Institution of Chemical Engineers.In a chemical looping combustor (CLC) system, the solid circulation rate (SCR) is a key parameter that determines the design, operati... [more]

© 2014 The Institution of Chemical Engineers.In a chemical looping combustor (CLC) system, the solid circulation rate (SCR) is a key parameter that determines the design, operating conditions and the overall efficiency of the system. In the present work, the gas-solid flow of a CLC cold flow model (10kWth) has been simulated by the computational fluid dynamics-discrete element method (CFD-DEM). The results showed that the SCR at different locations of the system fluctuates with time with different amplitude, and the variation of SCR is periodically stable. The turbulent gas-solid flow regime in the air reactor was found to be the main mechanism driving the fluctuation of SCR and determined the fluctuation frequency and amplitude. The SCR increased with the flow rates of air/fuel reactors and loop seals, and the total solid inventory. Changes in operating conditions directly induced the change in the mass of solids that were entrained into the riser from the air reactor and how fast the solids were transported therein. A correlation was subsequently proposed to describe the SCR as a function of solid hold-up and gas flow velocity in the riser. The particle residence time decreased in a power law as the SCR increased. Reasonable agreements were obtained between simulations and experiments in terms of solid distribution, gas-solid flow patterns, pressure drop profiles and SCR.

DOI 10.1016/j.cherd.2014.11.005
Citations Scopus - 7Web of Science - 6
Co-authors Behdad Moghtaderi, Kalpit Shah
2015 Peng Z, Doroodchi E, Sathe M, Joshi JB, Evans GM, Moghtaderi B, 'A method for calculating the surface area of numerically simulated aggregates', Advanced Powder Technology, 26 56-65 (2015) [C1]

© 2014 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.The success of many industrial processes... [more]

© 2014 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.The success of many industrial processes largely depends on the structural characteristics of aggregates. In intensive aerobic digestion process for wastewater treatment applications, the structural characteristics namely aggregate shape, size and therefore the aggregate surface area strongly influence the transfer of dissolved oxygen from the aeration process to aggregates of harmful contaminants/microorganisms. The aim of this study was to apply Discrete Element Modelling (DEM) techniques to the aggregation of suspended particles (microorganisms) to quantify the available surface area for convection and diffusion as a function of particles number concentration and surface charge. The simulation inputs included particle and fluid characteristics such as particle size and density, solid concentration, suspension pH and ionic strength. A post processing method based on the Go-chess concept was developed to quantify the surface area of aggregate structure. The simulation results showed that whilst an increase in connection points increases the total surface area of the aggregate, this does not necessarily translate into an increase in the surface area available for oxygen transfer as combinations of open and close pores are formed. Aggregate surface area was directly determined by aggregate structural characteristics, and increased rapidly when the coordination number was below 3.5 and the fractal dimension was less than 1.5. A correlation for prediction of aggregate external surface area was also proposed as a function of aggregate structural characteristics in terms of fractal dimension and coordination number.

DOI 10.1016/j.apt.2014.08.005
Citations Scopus - 2
Co-authors Behdad Moghtaderi, Geoffrey Evans
2015 Alghamdi Y, Peng Z, Shah K, Moghtaderi B, Doroodchi E, 'Predicting the solid circulation rate in chemical looping combustion systems using pressure drop measurements', Powder Technology, 286 572-581 (2015) [C1]

© 2015 Elsevier B.V.In chemical looping combustion systems, accurate measurement of the solid circulation rate (SCR) is crucial for optimising the system performance. Conventiona... [more]

© 2015 Elsevier B.V.In chemical looping combustion systems, accurate measurement of the solid circulation rate (SCR) is crucial for optimising the system performance. Conventionally, the SCR is predicted using the riser total pressure drop leading to an overestimation of up to 70%. In this work, a model has been proposed for the SCR prediction using the pressure drop at the top section of the riser. The height of this top section was determined by the riser gas-solid flow characteristics, namely, the axial solid holdup profile and lateral solid flux profile. A kinematic model was developed to predict the axial solid holdup profile and the reduced solid flux model developed by Rhodes et al. (1992) was employed to predict the mass fraction of upwards flowing solids. The prediction results of the proposed model were validated against the experimental data obtained in this work and those reported in the literature, where the prediction accuracy of SCR was significantly improved (by up to 60%) with a deviation of around 15%.

DOI 10.1016/j.powtec.2015.09.004
Citations Scopus - 2Web of Science - 2
Co-authors Behdad Moghtaderi, Kalpit Shah
2014 Peng Z, Doroodchi E, Luo C, Moghtaderi B, 'Influence of void fraction calculation on fidelity of CFD-DEM simulation of gas-solid bubbling fluidized beds', AIChE Journal, (2014) [C1]

The correct calculation of cell void fraction is pivotal in accurate simulation of two-phase flows using a computational fluid dynamics-discrete element method (CFD-DEM) approach.... [more]

The correct calculation of cell void fraction is pivotal in accurate simulation of two-phase flows using a computational fluid dynamics-discrete element method (CFD-DEM) approach. Two classical approaches for void fraction calculations (i.e., particle centroid method or PCM and analytical approach) were examined, and the accuracy of these methodologies in predicting the particle-fluid flow characteristics of bubbling fluidized beds was investigated. It was found that there is a critical cell size (3.82 particle diameters) beyond which the PCM can achieve the same numerical stability and prediction accuracy as those of the analytical approach. There is also a critical cell size (1/19.3 domain size) below which meso-scale flow structures are resolved. Moreover, a lower limit of cell size (1.63 particle diameters) was identified to satisfy the assumptions of CFD-DEM governing equations. A reference map for selecting the ideal computational cell size and the suitable approach for void fraction calculation was subsequently developed. © 2014 American Institute of Chemical Engineers.

DOI 10.1002/aic.14421
Citations Scopus - 16Web of Science - 13
Co-authors Behdad Moghtaderi
2014 Peng Z, Ghatage SV, Doroodchi E, Joshi JB, Evans GM, Moghtaderi B, 'Forces acting on a single introduced particle in a solid-liquid fluidised bed', Chemical Engineering Science, 116 49-70 (2014) [C1]

In a liquid fluidised bed system, the motion of each phase is governed by fluid-particle and particle-particle interactions. The particle-particle collisions can significantly aff... [more]

In a liquid fluidised bed system, the motion of each phase is governed by fluid-particle and particle-particle interactions. The particle-particle collisions can significantly affect the motion of individual particles and hence the solid-liquid two phase flow characteristics. In the current work, computational fluid dynamics-discrete element method (CFD-DEM) simulations of a dense foreign particle introduced in a monodispersed solid-liquid fluidised bed (SLFB) have been carried out. The fluidisation hydrodynamics of SLFB, settling behaviour of the foreign particle, fluid-particle interactions, and particle-particle collision behaviour have been investigated. Experiments including particle classification velocity measurements and fluid turbulence characterisation by particle image velocimetry (PIV) were conducted for the validation of prediction results. Compared to those predicted by empirical correlations, the particle classification velocity predicted by CFD-DEM provided the best agreement with the experimental data (less than 10% deviation). The particle collision frequency increased monotonically with the solid fraction. The dimensionless collision frequency obtained by CFD-DEM excellently fit the data line predicted by the kinetic theory for granular flow (KTGF). The particle collision frequency increased with the particle size ratio (dP2/dP1) and became independent of the foreign particle size for high solid fractions when the fluidised particle size was kept constant. The magnitude of collision force was 10-50 times greater than that of gravitational force and maximally 9 times greater than that of drag force. A correlation describing the collision force as a function of bed voidage was developed for Stp>65 and dP2/dP1=2. A maximum deviation of less than 20% was obtained when the correlation was used for the prediction of particle collision force. © 2014 Elsevier Ltd.

DOI 10.1016/j.ces.2014.04.040
Citations Scopus - 3Web of Science - 2
Co-authors Geoffrey Evans, Behdad Moghtaderi
2014 Azizian R, Doroodchi E, McKrell T, Buongiorno J, Hu LW, Moghtaderi B, 'Effect of magnetic field on laminar convective heat transfer of magnetite nanofluids', INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 68 94-109 (2014) [C1]
DOI 10.1016/j.ijheatmasstransfer.2013.09.011
Citations Scopus - 33Web of Science - 35
Co-authors Behdad Moghtaderi
2014 Zhou C, Doroodchi E, Moghtaderi B, 'Assessment of geothermal assisted coal-fired power generation using an Australian case study', ENERGY CONVERSION AND MANAGEMENT, 82 283-300 (2014) [C1]
DOI 10.1016/j.enconman.2014.03.011
Citations Scopus - 4Web of Science - 3
Co-authors Behdad Moghtaderi
2014 Zhang Y, Doroodchi E, Moghtaderi B, 'Chemical looping combustion of ultra low concentration of methane with Fe2O3/Al2O3 and CuO/SiO2', APPLIED ENERGY, 113 1916-1923 (2014) [C1]
DOI 10.1016/j.apenergy.2013.06.005
Citations Scopus - 22Web of Science - 21
Co-authors Behdad Moghtaderi
2014 Song H, Shah K, Doroodchi E, Moghtaderi B, 'Development of a Cu-Mg-Based Oxygen Carrier with SiO2 as a Support for Chemical Looping Air Separation', ENERGY & FUELS, 28 163-172 (2014) [C1]
DOI 10.1021/ef401485p
Citations Scopus - 14Web of Science - 14
Co-authors Kalpit Shah, Behdad Moghtaderi
2014 Song H, Shah K, Doroodchi E, Wall T, Moghtaderi B, 'Analysis on Chemical Reaction Kinetics of CuO/SiO2 Oxygen Carriers for Chemical Looping Air Separation', ENERGY & FUELS, 28 173-182 (2014) [C1]
DOI 10.1021/ef401487x
Citations Scopus - 17Web of Science - 14
Co-authors Terry Wall, Behdad Moghtaderi, Kalpit Shah
2014 Song H, Shah K, Doroodchi E, Wall T, Moghtaderi B, 'Reactivity of Al2O3- or SiO2-Supported Cu-, Mn-, and Co-based oxygen carriers for chemical looping air separation', Energy and Fuels, 28 1284-1294 (2014) [C1]

The chemical looping air separation (CLAS) is a novel method for producing high-purity oxygen, which can be effectively integrated to oxy-fuel power plants. CuO/Cu2O, Mn2O3/Mn3O 4... [more]

The chemical looping air separation (CLAS) is a novel method for producing high-purity oxygen, which can be effectively integrated to oxy-fuel power plants. CuO/Cu2O, Mn2O3/Mn3O 4, and Co3O4/CoO have been found to be the most thermodynamically suitable oxidation pairs for the CLAS process. In the current study, the reactivity and stability of these metal oxides were analyzed further. A total of six different oxygen carrier samples were prepared by the dry impregnation method on SiO2 and Al2O3 supports. Their redox behavior has been investigated in a thermogravimetric analyzer (TGA) at four different temperatures, i.e., 800, 850, 900, and 950 C, where the temperature-programmed oxygen release and oxidation were applied for 5 continuous cycles using nitrogen and air, respectively. The results indicate that, although relatively all oxygen carriers exhibited good reactivity, CuO/Cu2O with SiO2 and Co3O4/CoO with Al2O3 were found to be most stable. Furthermore, oxygen transport capacity (OTC) (%) and rate of oxygen transport (ROT) (% min-1) were calculated. It was found that Cu oxide with SiO 2 has the highest OTC of 4.77% as well as the highest ROT of 5.1 and 10.9% min-1 for oxygen release and oxidation, respectively, at 950 C. The CuO/SiO2 oxygen carrier also exhibited better stability for the 41 continuous cycle test, with only 10.3% loss in OTC compared to 22.3% for Co3O4/Al2O3. The grain size growth was found to be the key cause in the loss of OTC. The oxygen concentration in the outlet stream for the CuO/SiO2 oxygen carrier was measured in packed-bed experiments at different temperatures. It was observed that the oxygen concentration at the outlet of the reactor was consistent with the equilibrium values at studied temperatures. © 2014 American Chemical Society.

DOI 10.1021/ef402268t
Citations Scopus - 16Web of Science - 15
Co-authors Terry Wall, Behdad Moghtaderi, Kalpit Shah
2014 Zhang Y, Moghtaderi B, Doroodchi E, 'Utilization of ventilation air methane as an oxidizing agent in chemical looping combustion', Energy Conversion and Management, (2014) [C1]

Release of fugitive methane (CH) emissions from ventilation air in coal mines is a major source of greenhouse gas (GHG) emissions. Approximately 64% of methane emissions in coal m... [more]

Release of fugitive methane (CH) emissions from ventilation air in coal mines is a major source of greenhouse gas (GHG) emissions. Approximately 64% of methane emissions in coal mine operations are the result of VAM (i.e. ventilation air methane) which is difficult for use as a source of energy. A novel ancillary utilization of VAM was thereby proposed. In this proposal, the VAM was utilized instead of air as a feedstock to a chemical looping combustion (CLC) process of coal. In this case, FeO/FeO particles were shuttled between two interconnected reactors for combustion of syngas produced by an imbedded coal gasifier. The effect of VAM flow rate and methane concentration on the performance of CLC was analyzed thermodynamically using Aspen Plus software. Results indicated that the variations of air reactor temperature with VAM flow rate and methane concentration can be minimized as expected. The effect of temperature and inlet methane concentration on the conversion of CH was examined experimentally in a fixed bed reactor with the presence of particles of FeO/AlO. Not surprisingly, the reaction temperature put a significant influence on the conversion of CH. The conversion started at the temperature about 300 °C and the temperature to achieve full conversion was around 500 °C while the temperature in empty reactor between 665 °C and 840 °C. This is due to the catalytic effect of oxygen carriers (i.e. FeO/AlO) on the conversion of methane. Moreover, it was observed that the methane conversion rate decreased with the increase in inlet methane concentration while increasing with FeO loading content. © 2014 Elsevier Ltd. All rights reserved.

DOI 10.1016/j.enconman.2014.01.005
Citations Scopus - 5Web of Science - 6
Co-authors Behdad Moghtaderi
2014 Ghatage SV, Peng Z, Sathe MJ, Doroodchi E, Padhiyar N, Moghtaderi B, et al., 'Stability analysis in solid-liquid fluidized beds: Experimental and computational', Chemical Engineering Journal, 256 169-186 (2014) [C1]

In this study the transition from homogeneous to heterogeneous flow in a solid-liquid fluidized bed (SLFB) is examined both experimentally and numerically. The experimental appara... [more]

In this study the transition from homogeneous to heterogeneous flow in a solid-liquid fluidized bed (SLFB) is examined both experimentally and numerically. The experimental apparatus comprised a refractive index-matched SLFB, comprising 5. mm diameter borosilicate glass and sodium iodine solution, which allowed for both instantaneous particle image velocimetry of the liquid flow field and solids hold-up measurements to be undertaken for superficial liquid velocities in the range of 0.06-0.22. m/s. The motion of individual, spherical steel balls (with diameters 6, 7, 8, 9. mm) was then tracked as it settled through the fluidized bed for differing superficial liquid velocities. It was observed that, for all the steel balls covered in this work, there was a change in slope in their respective classification velocity curves at a superficial liquid velocity of 0.08. m/s. This value was very close to the critical velocity of 0.085. m/s predicted from 1-D linear stability analysis; and therefore deemed to be the critical condition that marked the transition from homogeneous to non-homogenous flow. It is proposed that the change in slope of the classification velocity curve is due to the encounter of the settling foreign particles with liquid bubbles whose presence marks the onset of heterogeneous flow. Additional computational analysis, involving both Eulerian-Eulerian (E-E) and Eulerian-Lagrangian (E-L) approaches, is used to confirm the presence of liquid bubbles at a critical liquid hold-up of 0.54, which corresponds to that predicted from 1-D linear stability analysis. In summary, the study has highlighted that experimentally the transition condition for a SLFB can be obtained simply by observing the behavior of the classification velocity of a single foreign particle at different superficial liquid velocities. This transition condition was found to agree with the 1D linear stability criterion, Eulerian-Eulerian CFD (3D) and Eulerian-Lagrangian DEM (3D) approaches. © 2014 Elsevier B.V.

DOI 10.1016/j.cej.2014.06.026
Citations Scopus - 4Web of Science - 1
Co-authors Geoffrey Evans, Behdad Moghtaderi
2013 Mitra S, Doroodchi E, Pareek V, Joshi J, Evans GM, 'Collision behaviour of a small spherical particle on a large stationary droplet', Proceedings. Chemeca 2013, (2013) [E1]
Citations Scopus - 2Web of Science - 1
Co-authors Geoffrey Evans, Subhasish Mitra
2013 Mitra S, Sathe MJ, Doroodchi E, Utikar R, Shah MK, Pareek V, et al., 'Droplet impact dynamics on a spherical particle', CHEMICAL ENGINEERING SCIENCE, 100 105-119 (2013) [C1]
DOI 10.1016/j.ces.2013.01.037
Citations Scopus - 12Web of Science - 12
Co-authors Geoffrey Evans, Subhasish Mitra
2013 Ghatage SV, Sathe MJ, Doroodchi E, Joshi JB, Evans GM, 'Effect of turbulence on particle and bubble slip velocity', CHEMICAL ENGINEERING SCIENCE, 100 120-136 (2013) [C1]
DOI 10.1016/j.ces.2013.03.031
Citations Scopus - 5Web of Science - 3
Co-authors Geoffrey Evans
2013 Doroodchi E, Zulfiqar H, Moghtaderi B, 'A combined experimental and theoretical study on laboratory-scale comminution of coal and biomass blends', POWDER TECHNOLOGY, 235 412-421 (2013) [C1]
DOI 10.1016/j.powtec.2012.10.054
Citations Scopus - 4Web of Science - 3
Co-authors Behdad Moghtaderi
2013 Peng Z, Doroodchi E, Alghamdi Y, Moghtaderi B, 'Mixing and segregation of solid mixtures in bubbling fluidized beds under conditions pertinent to the fuel reactor of a chemical looping system', Powder Technology, 235 823-837 (2013) [C1]

Performance of chemical looping combustion processes can be improved drastically by enhancing the overall redox characteristics of the system through the use of binary mixtures of... [more]

Performance of chemical looping combustion processes can be improved drastically by enhancing the overall redox characteristics of the system through the use of binary mixtures of oxygen carriers. However, binary mixtures of oxygen carrier particles are often found to differ in both size and density and therefore have the tendency to segregate under certain operating conditions.In this work, a numerical study was conducted to investigate the mixing and segregation behaviour of binary mixtures of particles with different sizes and densities in a bubbling fluidized bed under conditions pertinent to the fuel reactor of a cold flow model (i.e. a non-reacting replica) of a 10kWth chemical looping combustor. The motion of particles was tracked individually by discrete element model (DEM), whilst the gas flow was modelled by computational fluid dynamics (CFD). Gas-particle interactions were considered by a two-way coupling method. Further, a modified version of Lacey's method was developed to calculate the mixing index, taking into account both the heterogeneity of solids spatial distribution and particle size differences.Results showed that the modified Lacey's method provided very consistent and stable mixing indexes, proving to be effective for an in-situ quantitative description of mixing. It was also found that as the size ratio of the binary mixture of particles reduced, the mixing index increased indicating better mixing conditions. The agreement between the DEM/CFD model predictions and the experimental data was found to be satisfactory. The optimum conditions for mixing of binary mixtures appeared to be a function of bubble size, bubble rising rate and bubbling dynamics (e.g., splitting and coalescence). Application of the DEM/CFD model for prediction of layer inversion phenomenon in gas-solid fluidized beds was also demonstrated. © 2012 Elsevier B.V.

DOI 10.1016/j.powtec.2012.11.047
Citations Scopus - 13Web of Science - 12
Co-authors Behdad Moghtaderi
2013 Zhou C, Doroodchi E, Moghtaderi B, 'An in-depth assessment of hybrid solar-geothermal power generation', Energy Conversion and Management, 74 88-101 (2013) [C1]
DOI 10.1016/j.enconman.2013.05.014
Citations Scopus - 32Web of Science - 22
Co-authors Behdad Moghtaderi
2013 Doroodchi E, Sathe M, Evans G, Moghtaderi B, 'Liquid-liquid mixing using micro-fluidised beds', Chemical Engineering Research and Design, 91 2235-2242 (2013) [C1]

This study experimentally investigates the application of a solid-liquid micro-fluidised bed as a micro-mixing device. The experiments were performed in a borosilicate capillary t... [more]

This study experimentally investigates the application of a solid-liquid micro-fluidised bed as a micro-mixing device. The experiments were performed in a borosilicate capillary tube with an internal diameter of 1.2. mm (i.e. near the upper-limit dimension of a micro-fluidic system) using borosilicate particles with a mean diameter of 98 µm. Refractive index matching technique using sodium iodide solution was employed to achieve a transparent fluidised bed. Mixing performance of the micro-fluidised bed in terms of mixing time was investigated using a dye dilution technique. Experiments were carried out in the creeping flow regime at Reynolds numbers ranging between 0.27 and 0.72. It was demonstrated that the micro-fluidised bed mixing time sharply decreases as the Reynolds number increases. That is because at relatively high Reynolds numbers, the particle oscillation is stronger creating larger disturbances in the flow. The energy dissipation rate in micro fluidised bed was estimated to be four orders of magnitude less than other passive micro mixers which operate in the turbulent regime. It was also demonstrated that the ratio of mixing time and the energy dissipation rate for fluidised bed micro-mixer was comparable to K-M, Tangential IMTEK, and interdigital micro-mixers. However, the fluidised bed micro-mixer was found to operate at much lower Reynolds numbers compared to other passive mixers, with a mixing time of the order of few seconds. © 2013 The Institution of Chemical Engineers.

DOI 10.1016/j.cherd.2013.06.024
Citations Scopus - 1
Co-authors Behdad Moghtaderi, Geoffrey Evans
2013 Ismay MJL, Doroodchi E, Moghtaderi B, 'Effects of colloidal properties on sensible heat transfer in water-based titania nanofluids', Chemical Engineering Research and Design, 91 426-436 (2013) [C1]
DOI 10.1016/j.cherd.2012.10.005
Citations Scopus - 11Web of Science - 12
Co-authors Behdad Moghtaderi
2013 Alghamdi YA, Doroodchi E, Moghtaderi B, 'Mixing and segregation of binary oxygen carrier mixtures in a cold flow model of a chemical looping combustor', Chemical Engineering Journal, 223 772-784 (2013) [C1]

In a typical chemical looping combustion process, the oxygen for fuel combustion is supplied by circulating metal based oxygen carriers between two interconnected fluidised bed re... [more]

In a typical chemical looping combustion process, the oxygen for fuel combustion is supplied by circulating metal based oxygen carriers between two interconnected fluidised bed reactors. The redox characteristics of oxygen carriers and hence the overall performance of the process can be significantly improved by utilising binary mixtures of oxygen carrier particles. The full potential of such multi-species particle systems however can be only realised when particles segregation is minimised. This study is concerned with gaining an understanding of the mixing and segregation behaviour of binary mixtures of oxygen carrier particles with different sizes and densities in a cold flow model representing a 10. kWth chemical looping combustor. The hydrodynamics of such systems were investigated and compared with a typical chemical looping combustion process where single species are used. This was followed by investigating the solids mixing and segregation behaviour in terms of segregation intensity and species weight percentage at each reactor as a function of operating parameters. It was shown that increasing the total solid inventory, particle terminal velocity ratio, composition, and air reactor superficial velocity increases the riser pressure, solid circulation rates, and riser solid holdup. Mixing and segregation regimes of the fuel reactor and the component segregation between the two reactors were also mapped. The results showed that, for mixtures of species with low terminal velocity to high terminal velocity ratios of greater than 0.7, a good mixing in the fuel reactor can be achieved by maintaining the superficial gas velocity to the mixture minimum fluidisation velocity ratio above 5. For the tested conditions, the component segregation between the two reactors was avoided by maintaining the ratio of the riser superficial velocity to the terminal velocity of the species with a high terminal velocity between 1.25 and 2. © 2013 Elsevier B.V.

DOI 10.1016/j.cej.2013.03.037
Citations Scopus - 5Web of Science - 5
Co-authors Behdad Moghtaderi
2012 Doroodchi E, Peng Z, Sathe MJ, Abbasi Shavazi E, Evans GM, 'Fluidisation and packed bed behaviour in capillary tubes', Powder Technology, 223 131-136 (2012) [C1]
Citations Scopus - 10Web of Science - 10
Co-authors Geoffrey Evans
2012 Peng Z, Doroodchi E, Evans GM, 'Influence of primary particle size distribution on nanoparticles aggregation and suspension yield stress: A theoretical study', Powder Technology, 223 3-11 (2012) [C1]
Citations Scopus - 8Web of Science - 9
Co-authors Geoffrey Evans
2012 Moghtaderi B, Doroodchi E, 'Performance characteristics of a miniaturised chemical looping steam reformer for hydrogen enrichment of fuels', International Journal of Hydrogen Energy, 37 15164-15169 (2012) [C1]
Citations Scopus - 1Web of Science - 1
Co-authors Behdad Moghtaderi
2012 Song H, Doroodchi E, Moghtaderi B, 'Redox characteristics of Fe-Ni/SiO2 bimetallic oxygen carriers in CO under conditions pertinent to chemical looping combustion', Energy & Fuels, 26 75-84 (2012) [C1]
DOI 10.1021/ef201152u
Citations Scopus - 12Web of Science - 7
Co-authors Behdad Moghtaderi
2012 Azizian MR, Doroodchi E, Moghtaderi B, 'Effect of nanoconvection caused by Brownian Motion on the enhancement of thermal conductivity in nanofluids', Industrial & Engineering Chemistry Research, 51 1782-1789 (2012) [C1]
DOI 10.1021/ie201110k
Citations Scopus - 14Web of Science - 9
Co-authors Behdad Moghtaderi
2012 Cai Z, Gao Z, Bao Y, Evans GM, Doroodchi E, 'Formation and motion of conjunct bubbles in glycerol-water solutions', Industrial & Engineering Chemistry Research, 51 1990-1996 (2012) [C1]
Citations Scopus - 3Web of Science - 2
Co-authors Geoffrey Evans
2012 Peng Z, Doroodchi E, Moghtaderi B, Evans GM, 'A DEM-based analysis of the influence of aggregate structure on suspension shear yield stress', Advanced Powder Technology, 23 437-444 (2012) [C1]
Citations Scopus - 7Web of Science - 7
Co-authors Behdad Moghtaderi, Geoffrey Evans
2011 Zhang YX, Doroodchi E, Moghtaderi B, 'Thermodynamic assessment of a novel concept for integrated gasification chemical looping combustion of solid fuels', Energy & Fuels, 26 287-295 (2011) [C1]
DOI 10.1021/ef201156x
Citations Scopus - 31Web of Science - 24
Co-authors Behdad Moghtaderi
2011 Evans TM, Doroodchi E, Moghtaderi B, 'A response to Murshed et al., J Nanopart Res (2010) 12:2007-2010', Journal of Nanoparticle Research, 13 4395-4396 (2011) [C3]
DOI 10.1007/s11051-011-0431-y
Citations Scopus - 1Web of Science - 1
Co-authors Behdad Moghtaderi
2010 Peng Z, Doroodchi E, Evans GM, 'DEM simulation of aggregation of suspended nanoparticles', Powder Technology, 204 91-102 (2010) [C1]
DOI 10.1016/j.powtec.2010.07.023
Citations Scopus - 24Web of Science - 20
Co-authors Geoffrey Evans
2009 Doroodchi E, Evans T, Moghtaderi B, 'Comments on the effect of liquid layering on the thermal conductivity of nanofluids', Journal of Nanoparticle Research, 11 1501-1507 (2009) [C1]
DOI 10.1007/s11051-008-9522-9
Citations Scopus - 9Web of Science - 6
Co-authors Behdad Moghtaderi
2008 Doroodchi E, Evans GM, Schwarz MP, Lane GL, Shah NH, Nguyen AV, 'Influence of turbulence intensity on particle drag coefficients', Chemical Engineering Journal, 135 129-134 (2008) [C1]
DOI 10.1016/j.cej.2007.03.026
Citations Scopus - 20Web of Science - 19
Co-authors Geoffrey Evans
2008 Evans GM, Galvin KP, Doroodchi E, 'Introducing quantitative life cycle analysis into the chemical engineering curriculum', Education for Chemical Engineers, 3 E57-E65 (2008) [C1]
DOI 10.1016/j.ece.2008.01.003
Citations Scopus - 7
Co-authors Kevin Galvin, Geoffrey Evans
2008 Evans GM, Doroodchi E, Lane GL, Koh PTL, Schwarz MP, 'Mixing and gas dispersion in mineral flotation cells', Chemical Engineering Research and Design, 86 1350-1362 (2008) [C1]
DOI 10.1016/j.cherd.2008.07.006
Citations Scopus - 11Web of Science - 5
Co-authors Geoffrey Evans
2006 Doroodchi E, Zhou ZQ, Fletcher DF, Galvin KP, 'Particle size classification in a fluidized bed containing parallel inclined plates', Minerals Engineering, 19 162-171 (2006) [C1]
DOI 10.1016/j.mineng.2005.08.001
Citations Scopus - 15Web of Science - 15
Co-authors Kevin Galvin
2006 Moghtaderi B, Shames I, Doroodchi E, 'Combustion prevention of iron powders by a novel coating method', Chemical Engineering & Technology, 29 97-103 (2006) [C1]
DOI 10.1002/ceat.200500244
Citations Scopus - 8Web of Science - 7
Co-authors Behdad Moghtaderi
2005 Galvin KP, Callen AM, Zhou ZQ, Doroodchi E, 'Performance of the reflux classifier for gravity separation at full scale', Minerals Engineering, 18 19-24 (2005) [C1]
DOI 10.1016/j.mineng.2004.05.023
Citations Scopus - 33Web of Science - 25
Co-authors Kevin Galvin
2005 Doroodchi E, Galvin KP, Fletcher DF, 'The influence of inclined plates on expansion behaviour of solid suspensions in a liquid fluidised bed - a computational fluid dynamics study', Powder Technology, 156 1-7 (2005) [C1]
DOI 10.1016/j.powtec.2005.05.057
Citations Scopus - 24Web of Science - 22
Co-authors Kevin Galvin
2004 Doroodchi E, Fletcher DF, Galvin KP, 'Influence of inclined plates on the expansion behaviour of particulate suspensions in a liquid fluidised bed', Chemical Engineering Science, 59 3559-3567 (2004) [C1]
DOI 10.1016/j.ces.2004.05.020
Citations Scopus - 17Web of Science - 16
Co-authors Kevin Galvin
2002 Galvin KP, Doroodchi E, Callen AM, Lambert N, Pratten SJ, 'Pilot plant trial of the reflux classifier', Minerals Engineering, 15 19-25 (2002) [C1]
Citations Scopus - 34Web of Science - 27
Co-authors Kevin Galvin
Show 58 more journal articles

Conference (43 outputs)

Year Citation Altmetrics Link
2015 Khairul MA, Shah KV, Doroodchi E, Moghtaderi B, 'Application of nanofluids to enhance heat transfer in renewable energy systems', In: 3rd ASEAN Australian Engineering Congress (AAEC 2015) : Australian Engineering Congress on Innovative Technologies for Sustainable Development and Renewable Energy. Barton, ACT: Engineers Australia, 2015: 49-54. (2015) [E2]
Co-authors Mohammadkhairul Alam Uon, Kalpit Shah, Behdad Moghtaderi
2015 Khan M, Mitra S, Karim I, Ghatage S, Peng Z, Doroodchi E, et al., 'Bed Expansion Behaviour in a Binary Solid-Liquid Fluidised Bed with Different Initial Solid Loading- CFD Simulation and Validation', Eleventh International Conference on CFD in the Minerals and Process Industries (2015) [E1]
Co-authors Geoffrey Evans, Behdad Moghtaderi, Mdshakhaoath Khan Uon, Subhasish Mitra
2015 Peng Z, Doroodchi E, Moghtaderi B, Alghamdi Y, 'Analysis of Interaction Forces for Predicting the Transition from Segregation to Mixing of Binary Solids in a Miniaturised Gas Fluidised Bed', Asia Pacific Confederation of Chemical Engineering Congress 2015: APCChE 2015, incorporating CHEMECA 2015 (2015) [E1]
Co-authors Behdad Moghtaderi
2015 Khan M, Mitra S, Ghatage S, Peng Z, Doroodchi E, Moghtaderi B, et al., 'Expansion behavior of binary solid-liquid fluidised bed with different solid mass ratio' (2015) [E1]
Co-authors Subhasish Mitra, Geoffrey Evans, Behdad Moghtaderi, Mdshakhaoath Khan Uon
2015 Peng Z, Khan MD, Ghatage S, Doroodchi E, Moghtaderi B, Joshi J, Evans G, 'CFD-DEM simulation of binary systems of particles in liquid fluidised beds: segregation and dispersion' (2015) [E1]
Co-authors Behdad Moghtaderi, Geoffrey Evans, Mdshakhaoath Khan Uon
2014 Paymooni K, Doroodchi E, Moghtaderi B, 'Simulation of Perovskite membrane for integration into a chemical looping air separation unit', Chemical Engineering Transactions (2014) [E1]

Copyright © 2014, AIDIC Servizi S.r.l.The Chemical Looping Air Separation (CLAS) process was developed at the University of Newcastle for tonnage oxygen production. CLAS has a mu... [more]

Copyright © 2014, AIDIC Servizi S.r.l.The Chemical Looping Air Separation (CLAS) process was developed at the University of Newcastle for tonnage oxygen production. CLAS has a much lower energy intensity than conventional processes, requiring only 12 % of the specific power consumption; however, there are still some energy penalties associated with the CLAS process. The most significant being the large amounts of energy consumed in the steam generation and condensation processes. The aim of this study is to increase the energy efficiency of the CLAS process via membrane integration. If a high temperature oxygen transport membrane is introduced in the reduction reactor of the CLAS system, pure oxygen is produced without the need for a steam condenser. The most attractive oxygen transport membrane is Ba0.5Sr0.5Co0.8Fe0.2 (BSCF) owing to its high oxygen permeation flux. The BSCF membrane was utilised to study the oxygen permeation flux, oxygen recovery and energy saving of the integrated process compared to the typical CLAS process. A mathematical model was developed for the BSCF disk membrane to predict the oxygen permeation flux and oxygen recovery over a range of temperatures. Constants of the model were fitted using experimental data. The modelling results showed almost 10 % and 13 % energy savings in the low and high temperature membrane integrated CLAS processes over the typical CLAS, respectively.

DOI 10.3303/CET1439198
Citations Scopus - 1Web of Science - 1
Co-authors Behdad Moghtaderi
2013 Mitra SSK, Sathe MJ, Doroodchi E, Pareek V, Joshi JB, Evans GE, 'In-flight collision behaviour of droplets on a spherical particle falling under gravity', 8th World Conference on Experimental Heat Transfer, Fluid Mechanics, and Thermodynamics (2013) [E1]
Co-authors Geoffrey Evans, Subhasish Mitra
2013 Marveh F, Doroodchi E, Galvin KP, 'Experimental Validation of a Novel Model for Sediment Consolidation', Australiasian Particle Technology Society Student Conference 2013 (2013) [E3]
Co-authors Kevin Galvin
2013 Peng Z, Doroodchi E, Sathe M, Joshi J, Evans G, Moghtaderi B, 'A method for calculating the surface area of numerically simulated aggregates', Chemeca 2013 (2013) [E1]
Citations Web of Science - 1
Co-authors Geoffrey Evans, Behdad Moghtaderi
2013 Forghani M, Doroodchi E, Galvin KP, 'Universal Scaling of Consolidation in Batch Settling', Chemeca 2013 (2013) [E1]
Co-authors Kevin Galvin
2012 Mitra SS, Sathe MJ, Doroodchi E, Evans GM, 'Investigation of droplet evaporation in a bubbling fluidized bed', Ninth International Conference on Computational Fluid Dynamics in the Minerals and Process Industries (2012) [E1]
Co-authors Subhasish Mitra, Geoffrey Evans
2012 Remoroza AI, Moghtaderi B, Doroodchi E, 'CO2-EGS in hot dry rock: Preliminary results from CO2-rock interaction experiments', Proceedings, Thirty-Seventh Workshop on Geothermal Reservoir Engineering (2012) [E2]
Co-authors Behdad Moghtaderi
2012 Doroodchi E, Sathe MJ, Boyes AD, Evans GM, Moghtaderi B, 'Liquid-liquid mixing using micro-fluidised beds', Proceedings. 14th European Conference on Mixing (2012) [E1]
Citations Web of Science - 1
Co-authors Geoffrey Evans, Behdad Moghtaderi
2012 Alghamdi YAF, Peng Z, Doroodchi E, Moghtaderi B, 'CFD-DEM simulation of particle mixing and segregation in a chemical looping combustion system under cold flow conditions', 21st International Conference on Fluidized Bed Combustion (2012) [E1]
Co-authors Behdad Moghtaderi
2011 Evans GM, He Q, Doroodchi E, 'Optimisation of industrial gas-lift pumps', 12th International Conference Multiphase Flow In Industrial Plants (2011) [E3]
Co-authors Geoffrey Evans
2011 Peng Z, Doroodchi E, Evans GM, 'Influence of aggregate structure on suspension yield stress: a numerical study', Chemeca 2011: Engineering a Better World (2011) [E1]
Co-authors Geoffrey Evans
2011 Remoroza AI, Doroodchi E, Moghtaderi B, 'Modelling a complete C02-EGS power generation process', New Zealand Geothermal Workshop 2011 Proceedings (2011) [E2]
Co-authors Behdad Moghtaderi
2011 Zhou C, Doroodchi E, Munro I, Moghtaderi B, 'A feasibility study on hybrid solar-geothermal power generation', New Zealand Geothermal Workshop 2011 Proceedings (2011) [E1]
Co-authors Behdad Moghtaderi
2011 Weir AG, Moghtaderi B, Doroodchi E, 'Improved efficiency of the carrier gas process using gases other than air', PORT2011 Proceedings (2011) [E3]
Co-authors Behdad Moghtaderi
2011 Song H, Shah KV, Doroodchi E, Moghtaderi B, 'Thermogravimetric analysis of Ni0/Si02 oxygen carriers under CO/air environment for chemical looping combustion', Proceedings of the 11th Australian Combustion Symposium (2011) [E1]
Co-authors Behdad Moghtaderi, Kalpit Shah
2011 Remoroza AI, Moghtaderi B, Doroodchi E, 'Coupled wellbore and 3D reservoir simulation of a CO2 EGS', Proceedings: Thirty-Sixth Workshop on Geothermal Reservoir Engineering (2011) [E2]
Co-authors Behdad Moghtaderi
2010 Azizian MR, Doroodchi E, Moghtaderi B, 'The role of liquid layering on the enhancement of thermal conductivitiy in nanofluids', Proceedings of the 14th International Heat Transfer Conference (2010) [E1]
Citations Scopus - 1
Co-authors Behdad Moghtaderi
2010 Peng Z, Doroodchi E, Evans GM, 'The effect of primary particle size distribution on aggregation of nanoparticles: A numerical study', Australasian Chemical Engineering Conference (2010) [E1]
Co-authors Geoffrey Evans
2010 Abbasi Shavazi E, Doroodchi E, Evans GM, 'Fluidization and packed bed behaviour in capillary tubes', Chemeca 2010: Proceedings of the 40th Australasian Chemical Engineering Conference (2010) [E1]
DOI 10.1016/j.powtec.2011.08.011
Co-authors Geoffrey Evans
2010 Remoroza AI, Doroodchi E, Moghtaderi B, 'Corrosion inhibition of acid-treated geothermal brine - Results from pilot testing in Southern Negros, Philippines', Proceedings World Geothermal Congress 2010 (2010) [E1]
Co-authors Behdad Moghtaderi
2009 Moghtaderi B, Doroodchi E, 'An overview of GRANEX technology for geothermal power generation and waste heat recovery', Proceedings of the 2009 Australian Geothermal Energy Conference (2009) [E2]
Co-authors Behdad Moghtaderi
2009 Remoroza AI, Doroodchi E, Moghtaderi B, 'Power generation potential of SC-CO2 thermosiphon for engineered geothermal systems', Proceedings of the 2009 Australian Geothermal Energy Conference (2009) [E2]
Co-authors Behdad Moghtaderi
2009 Sathe MJ, Joshi JB, Doroodchi E, Roberts RH, Evans GM, 'Stereo PIV/Shadowgraphy used to study bubble characteristics in turbulent flows', Proceedings of the 8th International Symposium on Particle Image Velocimetry (2009) [E2]
Co-authors Geoffrey Evans
2008 Evans GM, Doroodchi E, Lane G, Koh P, Schwarz P, 'Mixing and gas dispersion in mineral flotation cells', Sixth International Symposium on Mixing in Industrial Process Industries: Scientific Program (2008) [E2]
Co-authors Geoffrey Evans
2007 Moghtaderi B, Doroodchi E, 'Production of hydrogen by catalytic steam gasification of biomass at low temperatures', 15th European Biomass Conference & Exhibition - From Research to Market Deployment. Proceedings of the International Conference (2007) [E1]
Co-authors Behdad Moghtaderi
2007 Evans GM, Galvin KP, Doroodchi E, 'Introducing quantitative life cycle analysis into the chemical engineering curriculum', CHEMECA 2007: Academia and Industry Strengthening the Profession. Proceedings (2007) [E1]
Co-authors Kevin Galvin, Geoffrey Evans
2007 Phan MC, Evans GM, Doroodchi E, Nguyen AV, Goodridge R, 'Breakup of a rectangular laminar jet in immiscible liquid-liquid systems', CHEMECA 2007: Academia and Industry Strengthening the Profession. Proceedings (2007) [E1]
Co-authors Geoffrey Evans
2006 Doroodchi E, Evans GM, Schwarz MP, Lane GL, Shah NH, Nguyen AV, 'Influence of turbulence intensity on particle drag coefficients', Process Intensification and Innovation Process (PI) Conference II - Cleaner, Sustainable, Efficient Technologies for the Future (2006) [E1]
Co-authors Geoffrey Evans
2006 Doroodchi E, Evans GM, Schwarz P, Lane G, Shah N, Nguyen AV, 'Particles drag coefficient in turbulent flows', Australian Workshop on Fluid Mechanics: A Complex Dynamical System (2006) [E2]
2004 Galvin KP, Doroodchi E, Callen AM, Moghtaderi B, Fletcher DF, Zhou ZQ, 'Development of a New Fluidized Bed Containing Inclined Plates', Proceedings, 12th International Conference on Transport & Sedimentation of Solid Particles (2004) [E1]
Co-authors Behdad Moghtaderi, Kevin Galvin
2004 Doroodchi E, Galvin KP, Fletcher DF, 'The Influence of Inclined Plates on Expansion Behaviour of Solid Suspensions in a Liquid Fluidised Bed - A Computational Fluid Dynamics Study', 32nd Australasian Chemical Engineering Conference (2004) [E1]
Citations Scopus - 7Web of Science - 3
Co-authors Kevin Galvin
2004 Doroodchi E, Zhou ZQ, Fletcher DF, Galvin KP, 'Influence of Inclined Plates on Separation Behaviour of Fluidised Suspensions - Enhanced Elutriation', Proceedings of the 11th International Conference on Fluidization (2004) [E1]
Co-authors Kevin Galvin
2004 Galvin KP, Callen AM, Zhou ZQ, Doroodchi E, 'Gravity Separation using a Full-Scale Reflux Classifier', Proceedings of the Tenth Australian Coal Preparation Conference (2004) [E1]
Co-authors Kevin Galvin
2002 Galvin KP, Belcher SM, Callen AM, Lambert N, Doroodchi E, Nguyen Tram Lam G, Pratten SJ, 'Gravity separation and hydrosizing using the reflux classifier', Proceedings of the Ninth Australian Coal Preparation Conference (2002) [E1]
Co-authors Kevin Galvin
2002 Doroodchi E, Fletcher DF, Galvin KP, 'Effect of inclined plates on separation behaviour of binary-solid particles in a liquid fluidised bed', Proceedings, World Congress on Particle Technology 4 (2002) [E1]
Co-authors Kevin Galvin
2001 Franks GV, Doroodchi E, 'Optimisation of biopolymer based gelcasting process for the production of advanced ceramic components', Proceedings, 6th World Congress of Chemical Engineering (2001) [E1]
2001 Galvin KP, Doroodchi E, Nguyentranlam G, Callen AM, Lambert N, Pratten SJ, 'Pilot plant hydrosizing trial of the reflux classifier' (2001) [E1]
2000 Galvin KP, Doroodchi E, 'Development of a novel crystallizer', 28th Australasian Chemical Engineering Conference (2000) [E1]
Co-authors Kevin Galvin
Show 40 more conferences

Patent (2 outputs)

Year Citation Altmetrics Link
2006 Moghtaderi B, Doroodchi E, A Method and System for Generating Power from a Heat Source (2006) [I3]
Co-authors Behdad Moghtaderi
2006 Moghtaderi B, Doroodchi E, Desalination Method and Apparatus (2006) [I3]
Co-authors Behdad Moghtaderi

Report (1 outputs)

Year Citation Altmetrics Link
2015 Moghtaderi B, Wall T, Doroodchi E, Shah K, Zhou C, Song H, 'Chemical Looping Oxygen Generation for Oxy-fuel Combustion: Final Report', Australian National Low Emissions Coal Research & Development, 94 (2015) [R1]
Co-authors Kalpit Shah, Behdad Moghtaderi, Terry Wall
Edit

Grants and Funding

Summary

Number of grants 25
Total funding $13,939,883

Click on a grant title below to expand the full details for that specific grant.


20142 grants / $5,460,000

Chemical Looping VAM Abatement Project$2,730,000

Funding body: ACALET (ACA Low Emissions Technologies Ltd)

Funding body ACALET (ACA Low Emissions Technologies Ltd)
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Doctor Kalpit Shah, Mr Jim Sandford
Scheme COAL21 Fund
Role Investigator
Funding Start 2014
Funding Finish 2017
GNo G1400521
Type Of Funding Grant - Aust Non Government
Category 3AFG
UON Y

Chemical Looping VAM Abatement Project$2,730,000

Funding body: ACALET (ACA Low Emissions Technologies Ltd)

Funding body ACALET (ACA Low Emissions Technologies Ltd)
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Doctor Kalpit Shah, Mr Jim Sandford
Scheme COAL21 Fund
Role Investigator
Funding Start 2014
Funding Finish 2017
GNo G1400521
Type Of Funding Grant - Aust Non Government
Category 3AFG
UON Y

20131 grants / $2,730,000

Chemical Looping VAM Abatement$2,730,000

Funding body: Department of Resources Energy and Tourism

Funding body Department of Resources Energy and Tourism
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Mr Jim Sandford
Scheme Coal Mining Abatement Technology Support Package (CMATSP)
Role Investigator
Funding Start 2013
Funding Finish 2016
GNo G1201041
Type Of Funding Other Public Sector - Commonwealth
Category 2OPC
UON Y

20123 grants / $120,000

Enhanced Carbon Removal in Secondary Steel Refining$90,000

Funding body: BlueScope Steel

Funding body BlueScope Steel
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi
Scheme Linkage Projects Partner Funding
Role Investigator
Funding Start 2012
Funding Finish 2014
GNo G1001084
Type Of Funding Aust Competitive - Commonwealth
Category 1CS
UON Y

3D Gamma Ray Tomography for Multiphase Flow Characterisation$20,000

Funding body: University of Newcastle

Funding body University of Newcastle
Project Team Dr Vishnu Pareek, Professor Geoffrey Evans, Associate Professor Elham Doroodchi, Doctor Roberto Moreno-Atanasio, Laureate Professor Graeme Jameson
Scheme Equipment Grant
Role Investigator
Funding Start 2012
Funding Finish 2012
GNo G1100626
Type Of Funding Internal
Category INTE
UON Y

Aeration of High Solids Concentration Wastewater Streams$10,000

Funding body: University of Newcastle - Faculty of Engineering & Built Environment

Funding body University of Newcastle - Faculty of Engineering & Built Environment
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi, Doctor Mayur Sathe
Scheme Pilot Grant
Role Investigator
Funding Start 2012
Funding Finish 2012
GNo G1200354
Type Of Funding Internal
Category INTE
UON Y

20112 grants / $280,000

Enhanced Carbon Removal in Secondary Steel Refining$230,000

Funding body: ARC (Australian Research Council)

Funding body ARC (Australian Research Council)
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi
Scheme Linkage Projects
Role Investigator
Funding Start 2011
Funding Finish 2014
GNo G1000973
Type Of Funding Aust Competitive - Commonwealth
Category 1CS
UON Y

Advanced Multiphase Flow Characterization Facility$50,000

Funding body: University of Newcastle

Funding body University of Newcastle
Project Team Dr Vishnu Pareek, Professor Geoffrey Evans, Professor Dongke Zhang, Assoc. Prof Aibing Yu, Professor Moses Tade, Dr Ranjeet Utikar, Laureate Professor Graeme Jameson, Laureate Professor Kevin Galvin, Associate Professor Elham Doroodchi
Scheme Equipment Grant
Role Investigator
Funding Start 2011
Funding Finish 2011
GNo G1000460
Type Of Funding Internal
Category INTE
UON Y

20107 grants / $1,738,000

High speed Particle Image Velocimetry and Laser-Induced Fluorescence Facility$495,000

Funding body: ARC (Australian Research Council)

Funding body ARC (Australian Research Council)
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi, Laureate Professor Kevin Galvin, Laureate Professor Graeme Jameson, Professor Mark Jones, Doctor Paul Stevenson, Professor Anh Nguyen, Professor Victor Rudolph, Dr Liguang Wang, Dr Zhi Ping Xu, Dr Vishnu Pareek, Dr Chi Phan, Professor Moses Tade, Dr Ranjeet Utikar, Assoc. Prof Aibing Yu, Dr Run Yang, Professor John Ralston, Associate Professor Stephen Grano
Scheme Linkage Infrastructure Equipment & Facilities (LIEF)
Role Investigator
Funding Start 2010
Funding Finish 2010
GNo G0190414
Type Of Funding Scheme excluded from IGS
Category EXCL
UON Y

Application of Tuneable Nanofluids in Regenerative Supercritical Power Generation$290,000

Funding body: ARC (Australian Research Council)

Funding body ARC (Australian Research Council)
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Mr Ian Munro
Scheme Linkage Projects
Role Investigator
Funding Start 2010
Funding Finish 2013
GNo G0900183
Type Of Funding Aust Competitive - Commonwealth
Category 1CS
UON Y

Application of Tuneable Nanofluids in Regenerative Supercritical Power Generation$240,000

Funding body: Granite Power Pty Ltd

Funding body Granite Power Pty Ltd
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Mr Ian Munro
Scheme Linkage Projects Partner Funding
Role Investigator
Funding Start 2010
Funding Finish 2012
GNo G0900200
Type Of Funding Grant - Aust Non Government
Category 3AFG
UON Y

Enhanced Waste Heat Recovery from Low-grade Heat Sources using a Novel Supercritical Power Cycle$228,000

Funding body: ARC (Australian Research Council)

Funding body ARC (Australian Research Council)
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Mr Ian Munro
Scheme Linkage Projects
Role Investigator
Funding Start 2010
Funding Finish 2011
GNo G0190488
Type Of Funding Aust Competitive - Commonwealth
Category 1CS
UON Y

High speed Particle Image Velocimetry and Laser-Induced Fluorescence Facility$185,000

Funding body: ARC (Australian Research Council)

Funding body ARC (Australian Research Council)
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi, Laureate Professor Kevin Galvin, Laureate Professor Graeme Jameson, Professor Mark Jones, Doctor Paul Stevenson, Professor Anh Nguyen, Professor Victor Rudolph, Dr Liguang Wang, Dr Zhi Ping Xu, Dr Vishnu Pareek, Dr Chi Phan, Professor Moses Tade, Dr Ranjeet Utikar, Assoc. Prof Aibing Yu, Dr Run Yang, Professor John Ralston, Associate Professor Stephen Grano
Scheme Linkage Infrastructure Equipment & Facilities (LIEF) Partner Funding
Role Investigator
Funding Start 2010
Funding Finish 2010
GNo G1000879
Type Of Funding Scheme excluded from IGS
Category EXCL
UON Y

Enhanced Waste Heat Recovery from Low-grade Heat Sources using a Novel Supercritical Power Cycle$150,000

Funding body: Granite Power Pty Ltd

Funding body Granite Power Pty Ltd
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi, Mr Ian Munro
Scheme Linkage Projects Partner Funding
Role Investigator
Funding Start 2010
Funding Finish 2011
GNo G0190508
Type Of Funding Aust Competitive - Commonwealth
Category 1CS
UON Y

High speed Particle Image Velocimetry and Laser-Induced Fluorescence Facility$150,000

Funding body: University of Newcastle

Funding body University of Newcastle
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi, Laureate Professor Kevin Galvin, Laureate Professor Graeme Jameson, Professor Mark Jones, Doctor Paul Stevenson, Professor Anh Nguyen, Professor Victor Rudolph, Dr Liguang Wang, Dr Zhi Ping Xu, Dr Vishnu Pareek, Dr Chi Phan, Professor Moses Tade, Dr Ranjeet Utikar, Assoc. Prof Aibing Yu, Dr Run Yang, Professor John Ralston, Associate Professor Stephen Grano
Scheme Equipment Grant
Role Investigator
Funding Start 2010
Funding Finish 2010
GNo G1000875
Type Of Funding Internal
Category INTE
UON Y

20082 grants / $385,300

Force Interactions inPacked andFluidised Beds at Micro-Scale Operation$380,000

Funding body: ARC (Australian Research Council)

Funding body ARC (Australian Research Council)
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi
Scheme Discovery Projects
Role Investigator
Funding Start 2008
Funding Finish 2010
GNo G0187525
Type Of Funding Aust Competitive - Commonwealth
Category 1CS
UON Y

State-of-the-Art in Power Cycles for Geothermal Applications and Bottoming Cycles$5,300

Funding body: Department of Primary Industries and Resources SA

Funding body Department of Primary Industries and Resources SA
Project Team Associate Professor Elham Doroodchi
Scheme Project Grant
Role Lead
Funding Start 2008
Funding Finish 2008
GNo G0189197
Type Of Funding Other Public Sector - State
Category 2OPS
UON Y

20076 grants / $3,169,402

A Novel Regenerator for Adapting Supercriticial Cycles to Geothermal Power Applications$2,449,000

Funding body: Newcastle Innovation

Funding body Newcastle Innovation
Project Team Professor Behdad Moghtaderi, Associate Professor Elham Doroodchi
Scheme Administered Research
Role Investigator
Funding Start 2007
Funding Finish 2009
GNo G0189884
Type Of Funding Internal
Category INTE
UON Y

2007 Research Fellowship - PRCAPP$621,441

Funding body: University of Newcastle

Funding body University of Newcastle
Project Team Associate Professor Elham Doroodchi
Scheme Research Fellowship
Role Lead
Funding Start 2007
Funding Finish 2013
GNo G0187098
Type Of Funding Internal
Category INTE
UON Y

Micro-Reactor production of Explosive Emulsions$61,961

Funding body: ORICA Australia Pty Ltd

Funding body ORICA Australia Pty Ltd
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi
Scheme Linkage Projects Partner Funding
Role Investigator
Funding Start 2007
Funding Finish 2007
GNo G0187402
Type Of Funding Contract - Aust Non Government
Category 3AFC
UON Y

2007 Research Fellowship Project Grant$15,000

Funding body: University of Newcastle

Funding body University of Newcastle
Project Team Associate Professor Elham Doroodchi
Scheme Fellowship Grant
Role Lead
Funding Start 2007
Funding Finish 2007
GNo G0188109
Type Of Funding Internal
Category INTE
UON Y

Processing of nano-particles using packed and fluidised beds$12,000

Funding body: University of Newcastle - Faculty of Engineering & Built Environment

Funding body University of Newcastle - Faculty of Engineering & Built Environment
Project Team

E Doroodchi

Scheme Independent Investigator Project Grant Scheme
Role Lead
Funding Start 2007
Funding Finish 2007
GNo
Type Of Funding Internal
Category INTE
UON N

Micro-Reactor production of Explosive Emulsions$10,000

Funding body: University of Newcastle

Funding body University of Newcastle
Project Team Professor Geoffrey Evans, Associate Professor Elham Doroodchi
Scheme Collaborative Research Grant
Role Investigator
Funding Start 2007
Funding Finish 2007
GNo G0187302
Type Of Funding Internal
Category INTE
UON Y

20062 grants / $57,181

MicroReactor Study$48,181

Funding body: ORICA Australia Pty Ltd

Funding body ORICA Australia Pty Ltd
Project Team Professor Geoffrey Evans, Associate Professor Anh Nguyen, Associate Professor Elham Doroodchi
Scheme ORICA Mining Chemicals Project
Role Investigator
Funding Start 2006
Funding Finish 2006
GNo G0186907
Type Of Funding Contract - Aust Non Government
Category 3AFC
UON Y

Hydrodynamics of Liquid Fluidisation at Micro-Scales$9,000

Funding body: University of Newcastle - Faculty of Engineering & Built Environment

Funding body University of Newcastle - Faculty of Engineering & Built Environment
Project Team

E Doroodchi

Scheme Independent Investigator Project Grant Scheme
Role Lead
Funding Start 2006
Funding Finish 2006
GNo
Type Of Funding Internal
Category INTE
UON N
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Research Supervision

Number of supervisions

Completed8
Current12

Total current UON EFTSL

Masters0.7
PhD2.95

Current Supervision

Commenced Level of Study Research Title / Program / Supervisor Type
2016 PhD Nanofluids Based Heat Sink for Cooling of Electronics Devices
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Principal Supervisor
2016 Masters A method for reducing pressure drop in solid-liquid micro-fluidized beds
M Philosophy (Chemical Eng), Faculty of Engineering and Built Environment, The University of Newcastle
Principal Supervisor
2016 Masters Development of a Novel Carbon Arrestor Process for Production of Designer Biochars
M Philosophy (Chemical Eng), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2016 PhD The Development of a Novel Microfluidic Assisted Ice Slurry Generator
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Principal Supervisor
2015 PhD Maximising Granulation Opportunity of Ironmaking Slag
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2014 PhD A Fundamental Study on Deflagration To Detonation Transition In Ventilation Air Methane
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2014 PhD Advanced Applications of Tunable Magnetite Nanofluids in Energy Systems and Energy Harvesters
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2013 PhD Application of Novel Calcium Looping Process for Providing CO2 and Heat to Greenhouses
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2013 PhD A Novel Ex-Situ Calcium Looping Process for Removal and Conversion of Tars Formed During Biomass Gasification
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2013 PhD Dispersion Behaviour in Binary Solid-Liquid Fluidized Beds
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2011 PhD A Fundamental Study on Membrane Integrated Chemical Looping Air Separation Process
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2011 PhD Instabilities and Hydrodynamic Origins of a Freely Moving Spherical Particle in Newtonian Fluid by Direct Numerical Simulation
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor

Past Supervision

Year Level of Study Research Title / Program / Supervisor Type
2016 PhD Transport Characteristics of Binary Mixture of Particles in Chemical Looping Combustion Applications
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Principal Supervisor
2016 PhD Droplet Particle Interaction in a Flowing Gas Stream
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2015 Masters Consolidation of Large Spherical Particles at Low Reynolds Numbers
M Philosophy (Chemical Eng), Faculty of Science and Information Technology, The University of Newcastle
Co-Supervisor
2015 Masters Consolidation of Large Spherical Particles at Low Reynolds Numbers
M Philosophy (Chemical Eng), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2014 PhD A Fundamental Study on Hybrid Geothermal Energy Systems
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2014 PhD Utilisation of Ventilation Air Methane in Chemical Looping Systems
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2013 PhD Application of Supercritical Carbon Dioxide in Engineered Geothermal System
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
2013 PhD A Fundamental Study on Heat Transfer Characteristics of Magnetite Nanofluids
PhD (Chemical Engineering), Faculty of Engineering and Built Environment, The University of Newcastle
Co-Supervisor
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News

GRANEX

Revolutionary clean energy technology launched in the Hunter

April 15, 2014

A new clean energy system launched today will demonstrate cost savings in electricity generation for remote mining and industrial sites and rural communities.

Professor Behdad Moghtaderi

World First Emissions Abatement Technology

February 20, 2014

The University of Newcastle has received $30 million to develop and roll-out world-leading abatement technologies for fugitive methane emissions from underground coal mining operations. The new technologies could reduce these emissions from the sector by as much as 90 percent and reduce Australia's annual greenhouse gas output by three percent.

Associate Professor Elham Doroodchi

Position

Associate Professor
School of Engineering
Faculty of Engineering and Built Environment

Focus area

Chemical Engineering

Contact Details

Email elham.doroodchi@newcastle.edu.au
Phone (02) 4033 9066
Fax (02) 4033 9095

Office

Room A235
Building NIER
Location Callaghan
University Drive
Callaghan, NSW 2308
Australia
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