Abstract

An extensive literature review of the mechanistic modeling of n-heptane and cyclohexane pyrolysis was carried out. It was shown that Rice–Kossiakoff free radical theory does not adequately account for product distributions of n-heptane pyrolysis in the high conversion regime. Secondary reactions of alpha higher olefins and di-olefins accounted for the major products (ethene, propene and 1-butene) of n-heptane pyrolysis. Predicted product distributions (CH4, C2H4, C3H6, 1-C4H8 and 1,3-C4H6) of n-heptane pyrolysis showed very good agreement with experimental data. The product distributions of cyclohexane pyrolysis in the high conversion regime were rationalized and adequately accounted for using decomposition reactions of cyclohexyl bi-radicals followed by secondary reactions of major primary products such as C3H6 and 1,3-C4H6. The latter expanded mechanism can be used to model cyclohexane pyrolysis in the high conversion regime. Rate parameters (pre-exponential factors and activation energy) for each of the elementary reactions of n-heptane mechanistic model were either obtained from the literature or estimated using thermochemical parameters. The use of steady state approximation in mathematical modeling of n-heptane pyrolysis led to erroneous results.

Highlights

  • Thermal decomposition of hydrocarbons is important in geothermal processes, conversion of petroleum oil, coal and biomass to liquid fuels, cracking of higher hydrocarbons to produce light olefins, degradation of endothermic jet fuels, and de-polymerization and recycling of synthetic polymers [1]

  • Most literature studies on hydrocarbons pyrolysis up to early 1980s were devoted to light paraffinic hydrocarbons because they result in high ethylene and propylene yields [2,3,4,5]

  • The present study is aimed at reviewing the literature on kinetics and mechanistic modeling of the pyrolysis of pure hydrocarbons and their mixtures under high conversion regime

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Summary

Introduction

Thermal decomposition of hydrocarbons is important in geothermal processes, conversion of petroleum oil, coal and biomass to liquid fuels, cracking of higher hydrocarbons to produce light olefins, degradation of endothermic jet fuels, and de-polymerization and recycling of synthetic polymers [1]. This technique has been used to give atomic description of initiation mechanisms and product distributions of the pyrolysis and combustion of hydrocarbons as well as provide robust molecular reaction mechanisms required for kinetic modeling. In modeling the thermal decomposition of hydrocarbons kinetic rate expressions are developed for radical and molecular species participating in the elementary reactions.

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