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The Effect of Catalyst Ratio on the Pyrolysis Yields for Waste Tyre

Received: 1 August 2018    Accepted: 19 August 2018    Published: 15 September 2018
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Abstract

This paper focus on the thermal pyrolysis of used tyre with different catalysts at a temperature 550°C and at a heating rate of 15°C/min. The effect of process parameters on liquid yield, char formation and volatiles were also studied. In the present work, thermal pyrolysis of waste tyre samples with two selected catalysts, namely Jordan zeolite (zeolite Jo) and activated alumina was carried out in a fixed-bed reactor. The catalyst was mixed with feedstock in different percentages (10%, 15%, 25% and 35% w/w). The effects of catalysts and their ratio on the pyrolysis product oil were investigated and the results were compared with the results of experiments performed without catalyst under the same conditions (temperature 550°C at a heating rate of 150C/min). The maximum liquid yield obtained from pyrolysis of waste tyre via catalyst were found as 49.32% and 51.54% on using activated alumina and zeolite Jo as catalysts, respectively, while these values were 42.48%, without catalyst. The mass loss of tyre was examined using the thermo gravimetric analysis profiles (TGA) at heating rate of 15°C/min in air atmosphere from room temperature up to 600°C. The tyre pyrolysis liquid product has been characterized including fuel properties, proximate analysis, and ultimate analysis and FTIR. Fuel properties show that it can be used as liquid fuels.

Published in American Journal of Chemical Engineering (Volume 6, Issue 4)
DOI 10.11648/j.ajche.20180604.14
Page(s) 60-64
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2024. Published by Science Publishing Group

Keywords

Catalysts, Waste Tyre, Zeolite, Pyrolysis, Bio-Oil

References
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Cite This Article
  • APA Style

    Falah Fahed Banihani, Zaid Falah Bani Hani. (2018). The Effect of Catalyst Ratio on the Pyrolysis Yields for Waste Tyre. American Journal of Chemical Engineering, 6(4), 60-64. https://doi.org/10.11648/j.ajche.20180604.14

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    ACS Style

    Falah Fahed Banihani; Zaid Falah Bani Hani. The Effect of Catalyst Ratio on the Pyrolysis Yields for Waste Tyre. Am. J. Chem. Eng. 2018, 6(4), 60-64. doi: 10.11648/j.ajche.20180604.14

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    AMA Style

    Falah Fahed Banihani, Zaid Falah Bani Hani. The Effect of Catalyst Ratio on the Pyrolysis Yields for Waste Tyre. Am J Chem Eng. 2018;6(4):60-64. doi: 10.11648/j.ajche.20180604.14

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  • @article{10.11648/j.ajche.20180604.14,
      author = {Falah Fahed Banihani and Zaid Falah Bani Hani},
      title = {The Effect of Catalyst Ratio on the Pyrolysis Yields for Waste Tyre},
      journal = {American Journal of Chemical Engineering},
      volume = {6},
      number = {4},
      pages = {60-64},
      doi = {10.11648/j.ajche.20180604.14},
      url = {https://doi.org/10.11648/j.ajche.20180604.14},
      eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20180604.14},
      abstract = {This paper focus on the thermal pyrolysis of used tyre with different catalysts at a temperature 550°C and at a heating rate of 15°C/min. The effect of process parameters on liquid yield, char formation and volatiles were also studied. In the present work, thermal pyrolysis of waste tyre samples with two selected catalysts, namely Jordan zeolite (zeolite Jo) and activated alumina was carried out in a fixed-bed reactor. The catalyst was mixed with feedstock in different percentages (10%, 15%, 25% and 35% w/w). The effects of catalysts and their ratio on the pyrolysis product oil were investigated and the results were compared with the results of experiments performed without catalyst under the same conditions (temperature 550°C at a heating rate of 150C/min). The maximum liquid yield obtained from pyrolysis of waste tyre via catalyst were found as 49.32% and 51.54% on using activated alumina and zeolite Jo as catalysts, respectively, while these values were 42.48%, without catalyst. The mass loss of tyre was examined using the thermo gravimetric analysis profiles (TGA) at heating rate of 15°C/min in air atmosphere from room temperature up to 600°C. The tyre pyrolysis liquid product has been characterized including fuel properties, proximate analysis, and ultimate analysis and FTIR. Fuel properties show that it can be used as liquid fuels.},
     year = {2018}
    }
    

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  • TY  - JOUR
    T1  - The Effect of Catalyst Ratio on the Pyrolysis Yields for Waste Tyre
    AU  - Falah Fahed Banihani
    AU  - Zaid Falah Bani Hani
    Y1  - 2018/09/15
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    N1  - https://doi.org/10.11648/j.ajche.20180604.14
    DO  - 10.11648/j.ajche.20180604.14
    T2  - American Journal of Chemical Engineering
    JF  - American Journal of Chemical Engineering
    JO  - American Journal of Chemical Engineering
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    EP  - 64
    PB  - Science Publishing Group
    SN  - 2330-8613
    UR  - https://doi.org/10.11648/j.ajche.20180604.14
    AB  - This paper focus on the thermal pyrolysis of used tyre with different catalysts at a temperature 550°C and at a heating rate of 15°C/min. The effect of process parameters on liquid yield, char formation and volatiles were also studied. In the present work, thermal pyrolysis of waste tyre samples with two selected catalysts, namely Jordan zeolite (zeolite Jo) and activated alumina was carried out in a fixed-bed reactor. The catalyst was mixed with feedstock in different percentages (10%, 15%, 25% and 35% w/w). The effects of catalysts and their ratio on the pyrolysis product oil were investigated and the results were compared with the results of experiments performed without catalyst under the same conditions (temperature 550°C at a heating rate of 150C/min). The maximum liquid yield obtained from pyrolysis of waste tyre via catalyst were found as 49.32% and 51.54% on using activated alumina and zeolite Jo as catalysts, respectively, while these values were 42.48%, without catalyst. The mass loss of tyre was examined using the thermo gravimetric analysis profiles (TGA) at heating rate of 15°C/min in air atmosphere from room temperature up to 600°C. The tyre pyrolysis liquid product has been characterized including fuel properties, proximate analysis, and ultimate analysis and FTIR. Fuel properties show that it can be used as liquid fuels.
    VL  - 6
    IS  - 4
    ER  - 

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Author Information
  • Department of Chemical Engineering, Albalqa Applied University, Alhuson, Jordan

  • Department of Civil Engineering, JUST University, Irbed, Jordan

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