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International Journal of Energy for a Clean Environment

Publicado 8 números por año

ISSN Imprimir: 2150-3621

ISSN En Línea: 2150-363X

SJR: 0.597 SNIP: 1.456 CiteScore™:: 3.7 H-Index: 18

Indexed in

CATALYTIC CRACKING OF PALM OIL: KINETIC STUDY

Volumen 8, Edición 1, 2007, pp. 65-79
DOI: 10.1615/InterJEnerCleanEnv.v8.i1.50
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SINOPSIS

The kinetics of the catalytic cracking of palm oil over steam-treated HZSM-5 zeolite is investigated using a fixed bed microreactor, operated at a temperature of 673−723 K, a weight hourly space velocity of 1−4 h−1, and a catalyst-to-oil ratio of 0.1−0.22. Lumped parameter models based on three, four, and six lumps were used sequentially to obtain the kinetic parameters. The cracking reaction was found to be first order, and the rate constants showed that gasoline and kerosene fractions did not undergo secondary cracking reactions compared with the diesel fraction. The predicted concentrations of products were found to be in agreement with the experimental values within the experimental error.

CITADO POR
  1. Taufiqurrahmi Niken, Bhatia Subhash, Catalytic cracking of edible and non-edible oils for the production of biofuels, Energy & Environmental Science, 4, 4, 2011. Crossref

  2. Twaiq Farouq, Nasser M. S., Onaizi Sagheer A., Langmuir–Hinshelwood kinetic study for palm oil catalytic cracking over Al-MCM-41, Reaction Kinetics, Mechanisms and Catalysis, 112, 2, 2014. Crossref

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