Issue 8, 2024

Pyrolysis and gasification of 5–20 mm tyre rubber cubes under carbon dioxide flow

Abstract

The thermal behaviour of waste tractor tyre tread was investigated using 5-, 10-, 15- and 20 mm cubes and video recording of the process – an experimental approach for which no precedent could be found in the literature. Pyrolysis and gasification under CO2 flow in the range of 400 °C to 1000 °C were studied using a pre-heated tube furnace under near-isothermal reaction conditions. The video-graphic timeline and thermal history observations were used to correlate the results with first-order heat-transfer calculations and TGA-derived kinetics published previously. For pyrolysis, heat-transfer becomes the rate limiting step in the region 800–900 °C and above. Experimental evidence shows that the full pyrolysis time may be estimated from the algebraic sum of the local kinetic component and a heat-transfer component. The pressure build-up due to the release of gaseous products results in shattering of the solid into sub-millimetre char fragments. The kinetics of the reverse-Boudouard reaction can be described by a standard gas–solid shrinking particle model; however the character of the charred remains complicates this. Mass transfer limits are predicted only to become significant above 1200 °C, for a well-characterised char surface.

Graphical abstract: Pyrolysis and gasification of 5–20 mm tyre rubber cubes under carbon dioxide flow

Supplementary files

Article information

Article type
Paper
Submitted
30 Oct 2023
Accepted
29 Apr 2024
First published
10 May 2024
This article is Open Access
Creative Commons BY-NC license

React. Chem. Eng., 2024,9, 2180-2196

Pyrolysis and gasification of 5–20 mm tyre rubber cubes under carbon dioxide flow

A. A. Jansen, J. S. Gama, I. J. van der Walt and P. L. Crouse, React. Chem. Eng., 2024, 9, 2180 DOI: 10.1039/D3RE00577A

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