Search Results - "Hla, San Shwe"

Towards Zero Emissions from Fossil Fuel Power Stations by Feron, Paul, Cousins, Ashleigh, Jiang, Kaiqi, Zhai, Rongrong, Shwe Hla, San, Thiruvenkatachari, Ramesh, Burnard, Keith

“…•The CO2-capture rate for fossil fuel fired power stations can be increased above 90% without major challenges in pre-, post-combustion and oxyfuel using a…”
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Characteristics of inorganic matter from Australian municipal solid waste processed under combustion and gasification conditions by Ilyushechkin, Alexander, He, Chong, Hla, San Shwe

“…The presence and composition of ash in solid waste streams produced by the thermochemical processes can affect the further disposal or use of the waste. This…”
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A study on a multi-stage hybrid gasifier-engine system by Bhattacharya, S.C, Shwe Hla, San, Pham, Hoang-Luang

“…This paper presents the results of a study on a multi-stage hybrid biomass–charcoal gasification to produce low tar content gas for engine application using…”
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Material Challenges and Hydrogen Embrittlement Assessment for Hydrogen Utilisation in Industrial Scale by Ilyushechkin, Alexander, Schoeman, Liezl, Carter, Lachlan, Hla, San Shwe

“…Hydrogen has been studied extensively as a potential enabler of the energy transition from fossil fuels to renewable sources. It promises a feasible…”
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Kinetics of high-temperature water-gas shift reaction over two iron-based commercial catalysts using simulated coal-derived syngases by Hla, San Shwe, Park, D., Duffy, G.J., Edwards, J.H., Roberts, D.G., Ilyushechkin, A., Morpeth, L.D., Nguyen, T.

“…The kinetics of the water-gas shift (WGS) reaction over two iron–chromium based commercial catalysts has been studied. The experiments were performed in a…”
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A CeO2–La2O3-based Cu catalyst for the processing of coal-derived syngases via high-temperature water–gas shift reaction by Hla, San Shwe, Morpeth, L.D., Sun, Y., Duffy, G.J., Ilyushechkin, A.Y., Roberts, D.G., Edwards, J.H.

“…A CeO2–La2O3-based Cu catalyst (referred to as CE09) has been tested in a differential reactor to measure its kinetics for the water–gas shift (WGS) reaction…”
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Kinetics of the water-gas shift reaction over a La0.7Ce0.2FeO3 perovskite-like catalyst using simulated coal-derived syngas at high temperature by SAN SHWE HLA, SUN, Y, DUFFY, G. J, MORPETH, L. D, ILYUSHECHKIN, A, COUSINS, A, ROBERTS, D. G, EDWARDS, J. H

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Effect of H2S on the performance of La0.7Ce0.2FeO3 perovskite catalyst for high temperature water–gas shift reaction by Morpeth, L.D., Sun, Y., Hla, San Shwe, French, D., Duffy, G.J., Edwards, J.H.

“…The effect of H2S on the performance of La0.7Ce0.2FeO3 perovskite catalyst was investigated for the production of hydrogen from simulated coal-derived syngas…”
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Characterisation of chemical composition and energy content of green waste and municipal solid waste from Greater Brisbane, Australia by Hla, San Shwe, Roberts, Daniel

“…•First detailed characterisation of Australian waste streams for energy recovery.•Chemical characteristics of green waste were similar to those of woody…”
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Ammonia decomposition kinetics over LiOH-promoted, α-Al2O3-supported Ru catalyst by Lamb, Krystina, Hla, San Shwe, Dolan, Michael

“…A LiOH-promoted Ru-based catalyst was recently reported to have a high TOF of 17.7 s−1 at 623 K, compared to 2.7 s−1 for an un-promoted Ru-based catalyst, and…”
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In situ measurements of solid-phase kinetic growth during slag isothermal crystallisation by He, Chong, Ilyushechkin, Alexander, Hla, San Shwe

“…•Kinetics of solid growth obtained by viscosity change during slag crystallisation.•Crystallisation rate is related to the viscosity and degree of…”
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The CO2 gasification reactivity of chars produced from Australian municipal solid waste by Hla, San Shwe, Lopes, Romain, Roberts, Daniel

“…•Detailed analysis of gasification behaviour of components of municipal waste.•Order of magnitude difference in CO2 gasification rates of different waste…”
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Catalysts for water-gas shift processing of coal-derived syngases by Hla, San Shwe, Duffy, G. J., Morpeth, L. D., Cousins, A., Roberts, D. G., Edwards, J. H., Park, D.

“…Although the gasification of coal is an efficient means of producing syngas, the carbon content of coal is such that gasification produces significantly higher…”
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Viscosity and crystallisation behaviour of coal ash slag from the primary phase of anorthite by He, Chong, Ilyushechkin, Alexander, Bai, Jin, Hla, San Shwe, Kong, Ling-Xue, Li, Wen

“…To achieve a stable slag-tapping process in entrained-flow coal gasifiers, the acceptable viscosity of coal ash slag is within 5–25 Pa·s in the temperature…”
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Viscosity of Spinel Primary Phase Field Slags from Australian Brown Coals by Ilyushechkin, Alexander, Kondratiev, Alex, He, Chong, Bai, Jin, Chen, Xiaodong, Hla, San Shwe

“…The achievement of a steady rate of slag tapping in entrained-flow gasifiers relies on their continuous, smooth operation. In turn, this requires the viscosity…”
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Effect of sodium in brown coal ash transformations and slagging behaviour under gasification conditions by Ilyushechkin, Alexander Y., Hla, San Shwe, Chen, Xiaodong, Roberts, Daniel G.

“…Alkali species in coal play an important role in mineral matter reactions during gasification. Brown coal ashes can be high in sodium (up to 20 wt%), which…”
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From laboratory-scale experiments to industrial-scale CFD simulations of entrained flow coal gasification by Vascellari, Michele, Roberts, Daniel G., Hla, San Shwe, Harris, David J., Hasse, Christian

“…•Four Australian coals characterized by laboratory-scale experiments.•Intrinsic char conversion model calibrated by experiments in zone II.•Char structural…”
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The CO 2 gasification reactivity of chars produced from Australian municipal solid waste by Hla, San Shwe, Lopes, Romain, Roberts, Daniel

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Viscosity of High-Iron Slags from Australian Coals by Ilyushechkin, Alexander Y, Hla, San Shwe

“…There is a need to characterize slag flow properties for continuous operation of entrained flow gasifiers at the expected slag tapping temperature range. Slag…”
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Modelling and experimental studies of a water–gas shift catalytic membrane reactor by Hla, San Shwe, Morpeth, Leigh D., Dolan, Michael D.

“…•A 2D-axisymmetric CMR model was developed using FLUENT.•There was close agreement between the model and the prototype.•Loading extra catalyst would lead to…”
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