2014
DOI: 10.1016/j.apenergy.2014.03.074
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FDI oriented modeling of an experimental SOFC system, model validation and simulation of faulty states

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Cited by 51 publications
(38 citation statements)
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“…The anode and the cathode channel dimensions of our cell are 0.45 mm × 0.45 mm. The value of Nusselt number from SOFC literature is ≈4.2 . Considering the fuel cell channel flow to be a fully developed laminar flow in a rectangular pipe, we have the following relation: italicNu=italichDhkf …”
Section: Preliminary Model Validationmentioning
confidence: 99%
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“…The anode and the cathode channel dimensions of our cell are 0.45 mm × 0.45 mm. The value of Nusselt number from SOFC literature is ≈4.2 . Considering the fuel cell channel flow to be a fully developed laminar flow in a rectangular pipe, we have the following relation: italicNu=italichDhkf …”
Section: Preliminary Model Validationmentioning
confidence: 99%
“…Because of the high number of uncertain parameters, model calibration is often performed for achieving compliance of the model predictions with the test results . However, no systematic method is followed in these works for the selection of the calibration parameters.…”
Section: Introductionmentioning
confidence: 99%
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“…Significant challenges arise in making SOFC systems responsive. Advanced integrated system controls, as explored in [15][16][17][18][19][20][21][22][23], are necessary in order to maintain system integrity, durability, and lifespan. Controller design is highly dependent upon the application requirements and system configuration, but generally thermal response should be damped to the extent possible, given the materials used and the high temperatures involved.…”
Section: Introductionmentioning
confidence: 99%
“…The importance of early detection, isolation, identification and possibly correction of faults, has been evidenced by previous research works on solid oxide fuel cell (SOFC) plants . With reference to the SOFC power plant scheme reported in (Figure , the possible types of faults have been grouped into four main categories (classes) , : (i) air leakage: this fault consists in leakage of air between the air blower and the SOFC stack itself; (ii) fuel leakage: in the reformer, the methane/steam feed is converted into a hydrogen rich mixture. Leakage is likely to occur between the exit of the reformer and the entrance of the SOFC stack because of the small dimensions and high diffusivity of the hydrogen molecule; (iii) SOFC stack degradation: an increase of the SOFC internal losses (activation, ohmic and diffusion losses) leads to a reduced electrochemical performance and efficiency.…”
Section: Introductionmentioning
confidence: 99%