This paper presents a semidetailed kinetic scheme for the oxidation of iso-octane (2,2,4-trimethyl-pentane). Both the low- and high-temperature primary mechanisms are reduced to a lumped kinetic model involving only a limited number of intermediate steps. This primary reaction scheme, similar to the one already presented for n-heptane [1], is flexible enough to maintain accurate prediction of intermediate components, heat release, and ignition delay times for a wide range of operating parameters. General criteria for the reduction of intermediate species allow an efficient coupling, with a detailed kinetic model of C1-C4 oxidation. Thermochemical oscillations and the negative temperature coefficient (NTC) region of the reaction rate of the low-temperature oxidation of iso-octane in a jet-stirred reactor are reproduced quite well by the model. Several comparisons with experimental data, obtained under very different operating conditions, including a shock tube, a rapid compression machine, flow and jet-stirred reactors, support the applicability of this model of iso-octane oxidation over a wide range of pressures, temperatures, and mixture compositions.

A wide-range modeling study of iso-octane oxidation

Ciajolo A
1997

Abstract

This paper presents a semidetailed kinetic scheme for the oxidation of iso-octane (2,2,4-trimethyl-pentane). Both the low- and high-temperature primary mechanisms are reduced to a lumped kinetic model involving only a limited number of intermediate steps. This primary reaction scheme, similar to the one already presented for n-heptane [1], is flexible enough to maintain accurate prediction of intermediate components, heat release, and ignition delay times for a wide range of operating parameters. General criteria for the reduction of intermediate species allow an efficient coupling, with a detailed kinetic model of C1-C4 oxidation. Thermochemical oscillations and the negative temperature coefficient (NTC) region of the reaction rate of the low-temperature oxidation of iso-octane in a jet-stirred reactor are reproduced quite well by the model. Several comparisons with experimental data, obtained under very different operating conditions, including a shock tube, a rapid compression machine, flow and jet-stirred reactors, support the applicability of this model of iso-octane oxidation over a wide range of pressures, temperatures, and mixture compositions.
1997
Istituto di Ricerche sulla Combustione - IRC - Sede Napoli
hydrocarbon oxidation
gasoline component combustion
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/291408
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