"Data from the thermal decomposition of bitumen from Utah tar sands was obtained and analysed with both isothermal and non-isothermal chemical reaction models. The use of a power rate law to describe the complex kinetics of pyrolysis gave agreement with the experimental data that was approximate, but adequate for design purposes. The results indicated a reaction rate that was second order in bitumen content, with an activation energy of about 17 to 20 kcal/gmol.
Data for the boiling point distribution of the products was consistent with a change of mechanism from vaporization to pyrolysis as the samples are heated. Higher heating rates gave a lower boiling product, with less contained sulfur, arsenic, and nitrogen. A chromatographic study of the types of compounds in the product indicated that pyrolysis begins at about 350°C. Approximately 20% of the bitumen was found to form coke during pyrolysis. The size of the tar sand particles was found to have a small effect on the rate of weight loss for the particle sizes studied.
Calculations of reactor volumes and process flow rates for a proposed bitumen pyrolysis/coke combustion process indicate the feasibility of using the coke combustion heat as the sole energy source. Study of the transient temperature behavior of a reacting tar sand pellet indicated that instantaneous heating is a satisfactory assumption for particles small enough to have small oxygen diffusion limitations on the combustion rate"--Abstract, page ii.
Liapis, Athanasios I.
Findley, Marshall E., 1927-1991
Crosser, Orrin K.
Poling, Bruce E.
Avula, Xavier J. R.
Chemical and Biochemical Engineering
Ph. D. in Chemical Engineering
University of Missouri at Rolla. Department of Chemical Engineering
Phillips Petroleum Company
Shell Oil Company
University of Missouri--Rolla
xii, 179 pages
© 1985 Charles Arthur Lechner, All rights reserved.
Dissertation - Restricted Access
Library of Congress Subject Headings
Pyrolysis -- Mathematical models
Oil sands extraction plants
Print OCLC #
Electronic OCLC #
Link to Catalog Record
Electronic access to the full-text of this document is restricted to Missouri S&T users. Otherwise, request this publication directly from Missouri S&T Library or contact your local library.http://laurel.lso.missouri.edu/record=b1764616~S5
Lechner, Charles Arthur, "Kinetics and reactor design in the pyrolysis of tar sands" (1985). Doctoral Dissertations. 581.
Share My Dissertation If you are the author of this work and would like to grant permission to make it openly accessible to all, please click the button above.