TY - GEN
T1 - Modeling and evaluation of an integrated microfluidic fuel processor for miniature power sources
AU - Qian, Dongying
AU - Besser, Ronald S.
AU - Lawal, Adeniyi
PY - 2006
Y1 - 2006
N2 - An integration scheme for a 20 w proton exchange membrane (PEM) fuel processor involving the steam reforming of methanol fuel was studied. The integration system incorporates four major components, i.e., vaporizer, reformer, preferential oxidation reactor and combustor, several internal heat exchangers, and some internal thermal barriers. A complete two-dimensional CFD simulation of the integrated system involving flow, heat and mass transfer as well as chemical reactions was performed. In this PEM fuel cell processing, the steam reforming was the slowest step, so the design of the steam reformer is the key for controlling the total size of the fuel processor. A high performance catalyst for the steam reformer was demanded. The thermal barriers between the processing units were critical for maintaining the temperature difference between the integrated components. Simulation results showed that these thermal barriers occupy a significant amount of the total space. A material with low thermal conductivity would help to reduce the total processor volume. Although in the process simulation, an isothermal condition for each reaction unit was assumed, the temperature in each processing unit was not constant after the thermal integration. The state and flow direction of the input streams, the size of the processing components, heat exchangers and thermal barriers were all determined from the CFD simulation. This is an abstract of paper presented at the AIChE Spring National Meeting (Orlando, FL 4/24-26/2006).
AB - An integration scheme for a 20 w proton exchange membrane (PEM) fuel processor involving the steam reforming of methanol fuel was studied. The integration system incorporates four major components, i.e., vaporizer, reformer, preferential oxidation reactor and combustor, several internal heat exchangers, and some internal thermal barriers. A complete two-dimensional CFD simulation of the integrated system involving flow, heat and mass transfer as well as chemical reactions was performed. In this PEM fuel cell processing, the steam reforming was the slowest step, so the design of the steam reformer is the key for controlling the total size of the fuel processor. A high performance catalyst for the steam reformer was demanded. The thermal barriers between the processing units were critical for maintaining the temperature difference between the integrated components. Simulation results showed that these thermal barriers occupy a significant amount of the total space. A material with low thermal conductivity would help to reduce the total processor volume. Although in the process simulation, an isothermal condition for each reaction unit was assumed, the temperature in each processing unit was not constant after the thermal integration. The state and flow direction of the input streams, the size of the processing components, heat exchangers and thermal barriers were all determined from the CFD simulation. This is an abstract of paper presented at the AIChE Spring National Meeting (Orlando, FL 4/24-26/2006).
KW - Fuel cell
KW - Integration
KW - Microreactor
KW - Modeling
UR - http://www.scopus.com/inward/record.url?scp=56549096938&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=56549096938&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:56549096938
SN - 0816910057
SN - 9780816910052
T3 - 2006 AIChE Spring Annual Meeting
BT - 2006 AIChE Spring Annual Meeting
T2 - 2006 AIChE Spring National Meeting
Y2 - 23 April 2006 through 27 April 2006
ER -