2000
DOI: 10.1016/s0894-1777(00)00041-8
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Announcement and call for papers third international conference on compact heat exchangers and enhancement technology for the process industries

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“…In order to consider the effect of CO or CO 2 , that can be present in the fuel if the stack is fed by a syngas, the adsorption, desorption and electro-oxidation of carbon monoxide and the reverse water gas shift reaction, which can take place in the anode side, are also considered, as investigated and analyzed in recent experimental and numerical studies [24][25][26][27][28][29][30][31][32]. Therefore, the anode activation overpotential is calculated by solving a set of equations, as described in Appendix B.…”
Section: Model Formulationmentioning
confidence: 99%
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“…In order to consider the effect of CO or CO 2 , that can be present in the fuel if the stack is fed by a syngas, the adsorption, desorption and electro-oxidation of carbon monoxide and the reverse water gas shift reaction, which can take place in the anode side, are also considered, as investigated and analyzed in recent experimental and numerical studies [24][25][26][27][28][29][30][31][32]. Therefore, the anode activation overpotential is calculated by solving a set of equations, as described in Appendix B.…”
Section: Model Formulationmentioning
confidence: 99%
“…The development of a cooling system, able to recover the thermal energy from the stack, is an important issue for a decentralized combined heat and power production in order to satisfy the thermal energy demand, while in a mobile or UPS application, the purpose of the cooling system is mainly to dissipate the heat at the same rate by which it is being produced, allowing the fuel cell stack to run steadily at a constant temperature [1][2][3][4][5][6]. …”
Section: Introductionmentioning
confidence: 99%