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Bulk features of catalytic co-pyrolysis of sugarcane bagasse and a hydrogen-rich waste: The case of waste heavy paraffin

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  • Kouhi, Masoumeh
  • Shams, Kayghobad

Abstract

In this study, catalytic and non-catalytic pyrolysis and co-pyrolysis of pretreated and intact sugarcane bagasse was investigated using waste heavy paraffin (as an in-situ supply of hydrogen). A Y-type commercial zeolite catalyst (HGY-A) which is a gasoline boosting catalyst suitable for hydrocracking reactions in oil refining was used for catalytic pyrolysis. Co-feeding of bagasse with paraffin produced higher liquid product yields and lower solid yields. The improved effective hydrogen to carbon ratio (H/Ceff) of the feedstock, and primary cracking and fragmentation reactions of heavy paraffin at temperatures around 600 °C are responsible for considerable improvement of bio-oil yield. Use of HGY-A catalyst did change the composition of the produced bio-oil; however, it did not have any appreciable impact on the bio-oil yield under various operational conditions. Results showed that acidic pretreatment of bagasse (with a 30% w/w HCl) reduced the bio-oil yield and increased the char yield.

Suggested Citation

  • Kouhi, Masoumeh & Shams, Kayghobad, 2019. "Bulk features of catalytic co-pyrolysis of sugarcane bagasse and a hydrogen-rich waste: The case of waste heavy paraffin," Renewable Energy, Elsevier, vol. 140(C), pages 970-982.
    • Handle: RePEc:eee:renene:v:140:y:2019:i:c:p:970-982
    DOI: 10.1016/j.renene.2019.03.115
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    References listed on IDEAS

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    1. Tamilselvi, R. & Ramesh, M. & Lekshmi, G.S. & Bazaka, Olha & Levchenko, Igor & Bazaka, Kateryna & Mandhakini, M., 2020. "Graphene oxide – Based supercapacitors from agricultural wastes: A step to mass production of highly efficient electrodes for electrical transportation systems," Renewable Energy, Elsevier, vol. 151(C), pages 731-739.

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