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Mechanisms and performance of coal burning Rijke type pulsating combustorsWang, Muh-Rong 05 1900 (has links)
No description available.
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Coal combustion in precessing jet flames / by Nikolaos Pandelis Megalos.Megalos, Nikolaos Pandelis January 1998 (has links)
Bibliography: leaves 369-382. / xxi, 382 leaves : ill. ; 30 cm. / Title page, contents and abstract only. The complete thesis in print form is available from the University Library. / Examines the potential of the PJ nozzle in the low NOx combustion of coal and is primarily concerned with application to cement kilns. / Thesis (Ph.D.)--University of Adelaide, Dept. of Chemical Engineering, 1998
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PREDICTION OF PARTICLE TRAJECTORIES IN OPPOSED FLOW FIELDS.Masteller, Melissa Mae. January 1984 (has links)
No description available.
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The control of fluidised combustorsGray, D. T. January 1986 (has links)
No description available.
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The hydrodynamics of circulating fluidized bedsHarris, Benjamin James January 1992 (has links)
No description available.
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AN EXPERIMENTAL STUDY OF COAL PYROLYSIS IN FLAT, LAMINAR OPPOSED FLOW COMBUSTION CONFIGURATIONS.Kram, Brian Howard. January 1984 (has links)
No description available.
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The monitoring of near burner slag formationTan, Chee Keong January 2002 (has links)
No description available.
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The formation and monitoring of gases associated with the spontaneous combustion of coalCooper, Malcolm January 1991 (has links)
No description available.
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Pyrolysis of Fine Coal Particles at High Heating Rate and PressureMill, Christopher John, School of Chemical Engineering & Industrial Chemistry, UNSW January 2000 (has links)
High-intensity pyrolysis, rapid heating in an inert gas atmosphere at up to 20 atm pressure, of 6 Australian coals was examined to gain further insight into high-intensity processes such as Integrated Gasification Combined Cycles (IGCC). Experiments focussed on pyrolysis in a specially developed Wire Mesh Reactor (WMR). The particle temperature lagged that of the mesh by 0.2 seconds at a heating rate of 100??~C s -1 and was predicted by modelling. This is part of the reason the volatile yield (VY) results for 10 s hold-time at ???b1.7 wt% daf of coal, is much more reproducible than 1 s hold-time experiments at ???b4.2 wt% daf of coal. Four coals of the same rank did not behave identically when heated. Three of the coals had a pyrolysis VY the same as the proximate VM when heated to 100??~C at 1 atm but the fourth, higher inertinite coal had a 1 atm pyrolysis VY 90% of its proximate VM. All four coals of similar rank had a significant decrease in VY, between 10 and 20 wt% daf of coal, with pressure increasing from 1 to 20 atm. The two lower rank coals showed less decrease in VY with increasing pressure than the higher rank and higher inertinite coals. The lower decrease in VY with increased pressure was mostly attributed to the lower inertinite levels for both the coals of similar rank and VM, and the coals of lower rank. Char characteristics examined focussed on pore Surface Area (SA). For high intensity WMR and Drop Tube Furnace (DTF) pyrolysis experiments CO2 SA for char from a particular coal was similar but the BET SA different. This was due to the char in the WMR experiments having longer to form larger pores determined by BET N2 SA. Both the N2 and CO2 SA was more than an order of magnitude greater than for low intensity pyrolysis char. This highlights that the WMR can be used to attain char with similar CO2 SA characteristics as other high intensity pyrolysis experiments and to provide a more meaningful insight into char reactivity than low intensity chars do.
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Ignition and combustion of pulverized coal particles injected by an opposed jet to a flat flame burnerNguyen, Luan Hoang 08 1900 (has links)
No description available.
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