SAE Technical Paper Series 2001
DOI: 10.4271/2001-01-0940
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A Modular Numerical Simulation Tool Predicting Catalytic Converter Light-Off by Improved Modeling of Thermal Management and Conversion Characteristics

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Cited by 22 publications
(7 citation statements)
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“…The thermal model simulates the heat transfers occurring in the DOC monolith and is used to predict the temperatures of both the solid and the gas. The thermal model is based on the work presented in the studies by Lubesky 19 and Buechner et al 20 and is a quasi-steady-state model, since it is based on the assumption that the characteristic time constant of the flow rate and temperature is much higher than the residence time of the flow. The convective heat transfer rate is calculated from the average gas temperature across the j th element (the DOC can be divided into four or five bricks, depending on the specific case) and the average solid temperature during the i th computational time step (Figure 6).…”
Section: The Doc Modelmentioning
confidence: 99%
“…The thermal model simulates the heat transfers occurring in the DOC monolith and is used to predict the temperatures of both the solid and the gas. The thermal model is based on the work presented in the studies by Lubesky 19 and Buechner et al 20 and is a quasi-steady-state model, since it is based on the assumption that the characteristic time constant of the flow rate and temperature is much higher than the residence time of the flow. The convective heat transfer rate is calculated from the average gas temperature across the j th element (the DOC can be divided into four or five bricks, depending on the specific case) and the average solid temperature during the i th computational time step (Figure 6).…”
Section: The Doc Modelmentioning
confidence: 99%
“…Based on the methodology outlined by Konstantinidis et al [3] and Buchner et al [4], a model was developed to solve non-steady conduction within metal pipe sections.…”
Section: Brief Model Overviewmentioning
confidence: 99%
“…In addition, the energy flows associated with conduction to the head and adjacent pipe section, with radiation and convection to the surroundings on the outer wall, and with convective heat transfer between the gas and inner wall of the section are included and solved via an energy balance including an energy storage term. Published relationships for free and forced convection to the surroundings [3][4][5] were included in the model. The degree of forced convection is dependent on the velocity of the air flowing over the pipe section as well as its wetted area.…”
Section: Brief Model Overviewmentioning
confidence: 99%
“…Based on the methodology outlined by Konstantinidis et al [3] and Buchner et al [4] a new model was developed to solve non-steady conduction within flanges and thick-walled sections but, because of the minimal impact on computation time, this approach was applied to all sections within the model regardless of wall thickness.…”
Section: Thick-walled Sections and Flangesmentioning
confidence: 99%