1985
DOI: 10.1016/0165-2370(85)80005-x
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High-temperature pyrolysis of ethanol

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1992
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Cited by 46 publications
(18 citation statements)
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“…The CH3CHOH radical is the dominant product at low temperatures ( [24,28,18,22]), but there is evidence ( [12,) that the branching ratios of C2H50H + X reactions shift at higher temperatures to favor the C2H40H and CH3CH20 radicals, as would be expected from bond energy considerations [29].…”
Section: Introductionmentioning
confidence: 92%
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“…The CH3CHOH radical is the dominant product at low temperatures ( [24,28,18,22]), but there is evidence ( [12,) that the branching ratios of C2H50H + X reactions shift at higher temperatures to favor the C2H40H and CH3CH20 radicals, as would be expected from bond energy considerations [29].…”
Section: Introductionmentioning
confidence: 92%
“…The static reactor studies, conducted between room temperature and 900 K ( [3][4][5]7]), observed significantly more acetaldehyde than ethene. However, the previous flow reactor studies of ethanol oxidation between 1100-1250 K ( [11,12]) found acetaldehyde and ethene in roughly equal abundance, and the diffusion flame study of Smith and Gordon [l] found more ethene than acetaldehyde by a factor of 3.…”
Section: Introductionmentioning
confidence: 97%
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“…Data have been reported from diffusion flame [4][5][6], static reactor [7][8][9][10][11][12], shock tube [13][14][15], flow reactor [16][17][18], and laminar premixed flame [19] experiments. Norton and Dryer [17,18] conducted a series of ethanol oxidation experiments in an Atmospheric Pressure Flow Reactor (APFR) and reported the evolution profiles of stable intermediates and reaction products.…”
Section: Introductionmentioning
confidence: 97%
“…Kinetic parameters for ethanol consumption were selected from different previous studies (Walker, 1977(Walker, , 1976Kerr and Parsonage, 1976;Tsang, 1976;Grotheer et al, 1986;Pitz et al, 1988). This mechanism was evaluated by comparison with experimental data coming from ethanol pyrolysis in a flow reactor (Rotzoll, 1985), from ethanol oxidation in a jet-stirred reactor (Dagaut et al, 1992), from ethanol-air flame burning velocities (Gü lder, 1982) and from ethanol-O 2 -Ar ignition delays measured in shock tubes (Natarajan and Bhaskaran, 1981;Simmie, 1991a, Dunphy et al 1991b). Marinov (1999) has developed a detailed chemical kinetic model representing the high temperature ethanol oxidation.…”
Section: Introductionmentioning
confidence: 99%