A review of mechanistic and mathematical modeling of n-heptane and cyclohexane pyrolysis

IF 0.125
David Stan Aribike, Alfred Akpoveta Susu
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引用次数: 6

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.

Abstract Image

正庚烷和环己烷热解机理及数学模型研究进展
对正庚烷和环己烷热解的机理建模进行了广泛的文献综述。结果表明,Rice-Kossiakoff自由基理论不能很好地解释正庚烷在高转化状态下的热解产物分布。α -高烯烃和二烯烃的二次反应是正庚烷热解的主要产物(乙烯、丙烯和1-丁烯)。预测的正庚烷热解产物分布(CH4、C2H4、C3H6、1- c4h8和1,3- c4h6)与实验数据吻合较好。利用环己基双自由基的分解反应,再加上C3H6和1,3- c4h6等主要初级产物的二次反应,对环己烷在高转化期的热解产物分布进行了合理的解释。后一种扩展机理可用于模拟环己烷在高转化状态下的热解。正庚烷各基本反应的速率参数(指前因子和活化能)可由文献求得,也可由热化学参数求得。采用稳态近似法对正庚烷热解过程进行数学建模,结果存在误差。
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来源期刊
Applied Petrochemical Research
Applied Petrochemical Research ENGINEERING, CHEMICAL-
自引率
0.00%
发文量
0
审稿时长
13 weeks
期刊介绍: Applied Petrochemical Research is a quarterly Open Access journal supported by King Abdulaziz City for Science and Technology and all the manuscripts are single-blind peer-reviewed for scientific quality and acceptance. The article-processing charge (APC) for all authors is covered by KACST. Publication of original applied research on all aspects of the petrochemical industry focusing on new and smart technologies that allow the production of value-added end products in a cost-effective way. Topics of interest include: • Review of Petrochemical Processes • Reaction Engineering • Design • Catalysis • Pilot Plant and Production Studies • Synthesis As Applied to any of the following aspects of Petrochemical Research: -Feedstock Petrochemicals: Ethylene Production, Propylene Production, Butylene Production, Aromatics Production (Benzene, Toluene, Xylene etc...), Oxygenate Production (Methanol, Ethanol, Propanol etc…), Paraffins and Waxes. -Petrochemical Refining Processes: Cracking (Steam Cracking, Hydrocracking, Fluid Catalytic Cracking), Reforming and Aromatisation, Isomerisation Processes, Dimerization and Polymerization, Aromatic Alkylation, Oxidation Processes, Hydrogenation and Dehydrogenation. -Products: Polymers and Plastics, Lubricants, Speciality and Fine Chemicals (Adhesives, Fragrances, Flavours etc...), Fibres, Pharmaceuticals.
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