1990
DOI: 10.1016/0009-2509(90)87150-q
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The choice between cooled tubular reactor models: analysis of the hot spot

Abstract: Abstract-The applicability of the one-dimensional pseudo-homogeneous model of the cooled tubular reactor is studied. Using the two-dimensional model as the more accurate one we compared both models by studying the influence of the design and operating variables on the conditions in the hot spot of the reactor. The effects were studied on an analytical basis, and a relation is derived that describes the radial temperature profile in the hot spot of the reactor. In the first section we present the model equation… Show more

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Cited by 12 publications
(4 citation statements)
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“…Parabolic radial temperature gradients are often found for packed-bed reactors, and in that case the temperature on the center axis of the reactor will always be higher than the average temperature. Experimentally, the temperature is measured on the center axis, whereas an ODM predicts the mean radial temperature over the cross-sectional area (see Westerink et al (1990)). As a consequence, the experimentally ob- Kaguei (1982)).…”
Section: Influence Of the Gas Velocitymentioning
confidence: 99%
“…Parabolic radial temperature gradients are often found for packed-bed reactors, and in that case the temperature on the center axis of the reactor will always be higher than the average temperature. Experimentally, the temperature is measured on the center axis, whereas an ODM predicts the mean radial temperature over the cross-sectional area (see Westerink et al (1990)). As a consequence, the experimentally ob- Kaguei (1982)).…”
Section: Influence Of the Gas Velocitymentioning
confidence: 99%
“…To simplify the calculations it is further assumed that radial concentration profiles are flat. According to calculations of Khanna and Seinfeld (1987) and Westerink et al (1990) this is an acceptable simplification under non-run-away conditions. Although concentrations are almost uniform over the radius, this does not apply to the reaction rates Ri because of the radial temperature profile.…”
Section: Model Equationsmentioning
confidence: 99%
“…The reactor considered in [1] is characterized by a stratified structure in the transversal direction and by the presence of volumetric heat generation by exothermic reactions. A special attention has been given in [1] to the occurrence of hot spots [2] and to the upper bounds of the existence domain of steady solutions [3], which represent in such processes the regime above of which the reactor becomes uncontrollable and thermal explosion may occur. The model calculations reported in [1] (and summarized in Section 2 below) apply to reactors encountered in the chemical process engineering, in civil engineering, combustion engineering, thermal explosion control and environmental energy engineering.…”
Section: Introductionmentioning
confidence: 99%