Author:
Chalov Kirill,Lugovoy Yury,Kosivtsov Yury,Sulman Mikhail,Sulman Esther,Valentina Matveeva Valentina Matveeva,Stepacheva Antonina
Abstract
<p>Basing on the experimental data the optimal parameters of the pyrolysis of heavy and residual hydrocarbons of oil were defined as follows: temperature of 500 °С; catalyst of CoCl<sub>2</sub> with the catalyst loading 5% (wt.) of the substrate weight. Under the optimal conditions the kinetic investigation of the pyrolysis process was carried out using the thermogravimetric method. According to the investigation, it was found that the activation energy of the catalytic pyrolysis of oil-containing waste decreased by 20-30 kJ/mol in comparison to non-catalytic process. Copyright © 2016 BCREC GROUP. All rights reserved</p><p><em>Received: 13<sup>th</sup> July 2015; Revised: 25<sup>th</sup> March 2016; Accepted: 1<sup>st</sup> April 2016</em></p><p><strong>How to Cite:</strong> Chalov, K., Lugovoy, Y., Kosivtsov, Y., Sulman, M., Sulman, E., Matveeva, V., Stepacheva, A. (2016). Kinetic Study of the Catalytic Pyrolysis of Oil-Containing Waste. <em>Bulletin of Chemical Reaction Engineering & Catalysis</em>, 11 (3): 330-338 (doi:10.9767/bcrec.11.3.572.330-338)</p><p><strong>Permalink/DOI:</strong> <a href="http://doi.org/10.9767/bcrec.11.3.572.330-338">http://doi.org/10.9767/bcrec.11.3.572.330-338</a></p>
Publisher
Bulletin of Chemical Reaction Engineering and Catalysis
Subject
Process Chemistry and Technology,Catalysis
Cited by
4 articles.
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