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Computational Analysis of Gas Flow and Heat Transport Phenomena in Ducts Relevant for Fuel Cells

Yuan, Jinliang LU (2003)
Abstract
The thesis concerns modeling, simulation and numerical analysis of heat and mass transport, and fluid flow in ducts of both solid oxide fuel cells (SOFCs) and proton exchange membrane fuel cells (PEMFCs). The unique fuel cell boundary conditions (thermal, mass) for the flow ducts in fuel cells are identified and applied. Various duct configurations have been studied, such as rectangular and trapezoidal cross sections, composite geometries including porous layer, flow duct and solid current inter-collector (-connector).



Numerical simulations of fully developed / developing laminar flow and heat transfer have been presented with various Gr*, Re, Rem, aspect ratio (b/h) and base angle at electrolyte supported SOFC boundary... (More)
The thesis concerns modeling, simulation and numerical analysis of heat and mass transport, and fluid flow in ducts of both solid oxide fuel cells (SOFCs) and proton exchange membrane fuel cells (PEMFCs). The unique fuel cell boundary conditions (thermal, mass) for the flow ducts in fuel cells are identified and applied. Various duct configurations have been studied, such as rectangular and trapezoidal cross sections, composite geometries including porous layer, flow duct and solid current inter-collector (-connector).



Numerical simulations of fully developed / developing laminar flow and heat transfer have been presented with various Gr*, Re, Rem, aspect ratio (b/h) and base angle at electrolyte supported SOFC boundary conditions. It was verified that the mass injection through one wall increases the friction factor f and decreases the Nusselt number Nu; the mass suction decreases f but Nu increases. Onset of deviation of friction factor and heat transfer from pure forced convection is caused by the formation of a vortex. It was verified that the number of vortices and enhancement of f and Nu depends mainly on the magnitude of Ratio of Gr*/Re2.



For the same design, combined effects of mass transfer and buoyancy force have been simulated for various Grashof number Gr*, mass suction rate Rem and Reynolds number Re. It was found that onset of gas flow and heat transfer from pure forced convection is caused by combined effects of the formation of vortices associated with buoyancy and downward flow with mass suction. The mass suction can advance the onset of instability for the combined flow



For the same design, combined effects of mass transfer and buoyancy force have been simulated for various Grashof number Gr*, mass suction rate Rem and Reynolds number Re. It was found that onset of gas flow and heat transfer from pure forced convection is caused by combined effects of the formation of vortices associated with buoyancy and downward flow with mass suction. The mass suction can advance the onset of instability for the combined flow relative to pure forced convection flow at all Reynolds numbers. The effect of combined flow on the friction factor is less significant than on the heat transfer. From the simulated velocity distribution in the PEMFC composite ducts, it was found that the velocity in the porous diffusion layer is only about a few percent of that in the gas flow duct, and secondary flows caused by mass transfer can be clearly found in both diffusion layer and gas flow duct. It was also found, among the parameters studied, that permeability and thermal conductivity ratio have a significant impact on f and Nu for both cathode and anode ducts at a fixed porous layer configuration.



It has been revealed that the values of fRe and Nu vary widely in anode-supported SOFC ducts, where the thickness of the porous layer is large. fRe decreases from that of pure duct flow and has a low value due to the permeation effects in the entrance. By varying one or more of the characteristic ratios identified in this study, effects of permeation and secondary flow on the gas flow and heat transfer have been investigated in terms of fRe and Nu. A uniform fRe in the main flow direction can be achieved through appropriate adjustment of the flow parameters or / and duct configuration. Based on the concentration prediction, it has been found that gas species transport from/to the reaction site is mainly dominated by mass convection in the entrance region and by species mass concentration associated diffusion after a certain distance downstream the inlet; The position for occurrence of this change depends on several parameters, e.g., the current density. (Less)
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author
supervisor
opponent
  • Dr Beale, Steven, Canada
organization
publishing date
type
Thesis
publication status
published
subject
keywords
Thermal engineering, applied thermodynamics, Termisk teknik, termodynamik, PEMFC., SOFC, CFD, Duct, Transport Process, Fuel Cell, Heat Transfer, Gas Flow, Numerical Simulation, Analysis
pages
180 pages
publisher
Jinliang Yuan, Division of Heat Transfer,
defense location
Sal M:E, M-huset, Ole Römers väg 1, Lunds Tekniska Högskola
defense date
2003-02-21 10:15:00
ISBN
91-628-5540-9
language
English
LU publication?
yes
additional info
Article: 1. J. Yuan, M. Rokni, B. Sundén, Simulation of Fully Developed Laminar Heat and Mass Transfer in Fuel Cell Ducts with Different Cross Sections, Int. J. Heat Mass Transfer 44 (2001) 4047-4058.2. J. Yuan, M. Rokni, B. Sundén, Buoyancy Effects on Developing Laminar Gas Flow and Heat Transfer in a Rectangular Fuel Cell Duct, Num. Heat Transfer (part A) 39 (2001) 801-822. Article: 3. J. Yuan, M. Rokni, and B. Sundén, Combined Mass Suction and Buoyancy Effects on Heat Transfer and Gas Flow in a Fuel Cell Duct, Num. Heat Transfer (in press) 2003. Article: 4. J. Yuan, M. Rokni, and B. Sundén, A Numerical Investigation of Gas Flow and Heat Transfer in Proton Exchange Membrane Fuel Cells, Num. Heat Transfer (accepted for publication) 2002. Article: 5. J. Yuan, M. Rokni, B. Sundén, Analysis of Fluid Flow and Heat Transfer for Proton Exchange Membrane Fuel Cells by an Extended Darcy Model, in: Progress in Transport Phenomena, S. Dost, H. Struchtrup, and I. Dincer (Eds), 837-842, Elsevier, 2002. Article: 6. J. Yuan, M. Rokni, and B. Sundén, Three-Dimensional Computational Analysis of Gas and Heat Transport Phenomena in Ducts Relevant for Anode-Supported Solid Oxide Fuel Cells, Int. J. Heat Mass Transfer 46 (2003) 809-821. 7. J. Yuan, M. Rokni, B. Sundén, Gas Flow and Heat Transfer Analysis for an Anode Duct in Reduced Temperature SOFCs, submitted to First International Conference on Fuel Cell Science, Engineering and Technology, April 21-23, 2003, Rochester, New York, USA.
id
7b8c6bbc-41a6-40f4-afdc-705a2d37dc57 (old id 465420)
date added to LUP
2016-04-01 16:09:48
date last changed
2018-11-21 20:39:13
@phdthesis{7b8c6bbc-41a6-40f4-afdc-705a2d37dc57,
  abstract     = {The thesis concerns modeling, simulation and numerical analysis of heat and mass transport, and fluid flow in ducts of both solid oxide fuel cells (SOFCs) and proton exchange membrane fuel cells (PEMFCs). The unique fuel cell boundary conditions (thermal, mass) for the flow ducts in fuel cells are identified and applied. Various duct configurations have been studied, such as rectangular and trapezoidal cross sections, composite geometries including porous layer, flow duct and solid current inter-collector (-connector).<br/><br>
<br/><br>
Numerical simulations of fully developed / developing laminar flow and heat transfer have been presented with various Gr*, Re, Rem, aspect ratio (b/h) and base angle at electrolyte supported SOFC boundary conditions. It was verified that the mass injection through one wall increases the friction factor f and decreases the Nusselt number Nu; the mass suction decreases f but Nu increases. Onset of deviation of friction factor and heat transfer from pure forced convection is caused by the formation of a vortex. It was verified that the number of vortices and enhancement of f and Nu depends mainly on the magnitude of Ratio of Gr*/Re2.<br/><br>
<br/><br>
For the same design, combined effects of mass transfer and buoyancy force have been simulated for various Grashof number Gr*, mass suction rate Rem and Reynolds number Re. It was found that onset of gas flow and heat transfer from pure forced convection is caused by combined effects of the formation of vortices associated with buoyancy and downward flow with mass suction. The mass suction can advance the onset of instability for the combined flow<br/><br>
<br/><br>
For the same design, combined effects of mass transfer and buoyancy force have been simulated for various Grashof number Gr*, mass suction rate Rem and Reynolds number Re. It was found that onset of gas flow and heat transfer from pure forced convection is caused by combined effects of the formation of vortices associated with buoyancy and downward flow with mass suction. The mass suction can advance the onset of instability for the combined flow relative to pure forced convection flow at all Reynolds numbers. The effect of combined flow on the friction factor is less significant than on the heat transfer. From the simulated velocity distribution in the PEMFC composite ducts, it was found that the velocity in the porous diffusion layer is only about a few percent of that in the gas flow duct, and secondary flows caused by mass transfer can be clearly found in both diffusion layer and gas flow duct. It was also found, among the parameters studied, that permeability and thermal conductivity ratio have a significant impact on f and Nu for both cathode and anode ducts at a fixed porous layer configuration.<br/><br>
<br/><br>
It has been revealed that the values of fRe and Nu vary widely in anode-supported SOFC ducts, where the thickness of the porous layer is large. fRe decreases from that of pure duct flow and has a low value due to the permeation effects in the entrance. By varying one or more of the characteristic ratios identified in this study, effects of permeation and secondary flow on the gas flow and heat transfer have been investigated in terms of fRe and Nu. A uniform fRe in the main flow direction can be achieved through appropriate adjustment of the flow parameters or / and duct configuration. Based on the concentration prediction, it has been found that gas species transport from/to the reaction site is mainly dominated by mass convection in the entrance region and by species mass concentration associated diffusion after a certain distance downstream the inlet; The position for occurrence of this change depends on several parameters, e.g., the current density.},
  author       = {Yuan, Jinliang},
  isbn         = {91-628-5540-9},
  language     = {eng},
  publisher    = {Jinliang Yuan, Division of Heat Transfer,},
  school       = {Lund University},
  title        = {Computational Analysis of Gas Flow and Heat Transport Phenomena in Ducts Relevant for Fuel Cells},
  year         = {2003},
}