21 |
Pyrolysis studies of synthetic polymers by mass spectrometry and othermethodsChan, Kit-ha, 陳潔霞 January 1984 (has links)
published_or_final_version / Chemistry / Doctoral / Doctor of Philosophy
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Effects of hydrogen on the coking of heavy hydrocarbon feedstocksBradley, A. J. January 1984 (has links)
No description available.
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23 |
Utilisation of Jordanian oil shales and predicted environmental impactsJaber, Jamal Othman January 1999 (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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Flash pyrolytic generation of xylylene derivativesRandles, K. R. January 1986 (has links)
No description available.
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An investigation of kerogens using pyrolysis methodsEglington, T. I. January 1988 (has links)
No description available.
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Rapid pyrolysis of celluloseHajaligol, Mohammad R January 1981 (has links)
Thesis (Ph.D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1981. / MICROFICHE COPY AVAILABLE IN ARCHIVES AND SCIENCE / Includes bibliographical references. / by Mohammad R. Hajaligol. / Ph.D.
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An optical study of soot formation from shock-induced benzene pyrolysisNelson, Greg January 2011 (has links)
Typescript (photocopy). / Digitized by Kansas Correctional Industries
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29 |
Applications of Py-GCMS to the study of maillard reaction : mechanistic and food quality aspectsWnorowski, Andrzej January 2003 (has links)
No description available.
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30 |
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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