1998
DOI: 10.1007/bf02672812
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Determination of global parameters of gas-phase oxidation reactions from heat-evolution rates in a plug flow reactor

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“…The preexponential factor A = 10 14 s −1 (m 3 /kg) a+b −1 (3.27 × 10 15 s −1 (m 3 /Kmol) a+b −1 ), the activation energy E a = 241.5 kJ/mole, and the fuel and oxygen concentration exponents a = 0.92 and b = 0.89 are for a one-step overall reaction of n-butanol that was obtained experimentally by Lisochkin and Pnznyak [23]. These parameters; however, led to a very large reaction rate and respectively a large heat release rate compared with that for other hydrocarbons (i.e, for n-heptane A = 3.35 × 10 11 s −1 (m 3 /kmol.s) a+b −1 , E a = 153 kJ/mole and a = b = 1 [24].…”
Section: Mathematical Modelmentioning
confidence: 96%
“…The preexponential factor A = 10 14 s −1 (m 3 /kg) a+b −1 (3.27 × 10 15 s −1 (m 3 /Kmol) a+b −1 ), the activation energy E a = 241.5 kJ/mole, and the fuel and oxygen concentration exponents a = 0.92 and b = 0.89 are for a one-step overall reaction of n-butanol that was obtained experimentally by Lisochkin and Pnznyak [23]. These parameters; however, led to a very large reaction rate and respectively a large heat release rate compared with that for other hydrocarbons (i.e, for n-heptane A = 3.35 × 10 11 s −1 (m 3 /kmol.s) a+b −1 , E a = 153 kJ/mole and a = b = 1 [24].…”
Section: Mathematical Modelmentioning
confidence: 96%