Thermal Science and Engineering
Online ISSN : 1882-2592
Print ISSN : 0918-9963
ISSN-L : 0918-9963
Volume 18 , Issue 3
Showing 1-2 articles out of 2 articles from the selected issue
  • Hitoshi MATSUSHIMA, Hiroshige KIKUCHI, Tadakatsu NAKAJIMA, Noboru OSHI ...
    2010 Volume 18 Issue 3 Pages 93-102
    Published: 2010
    Released: November 03, 2010
    JOURNALS FREE ACCESS
    Simulator for air cooled chillers that is able to handle the wide range of operating conditions is developed. Using this simulator, identification of performance characteristics of chillers is conducted. The simulator predicts the performance of chillers with practical accuracy after adjusting the component specifications and cycle conditions to meet the performance at the standard operational conditions in a catalog. Data-based subprogram that is based on the multi-dimensional data for operational characteristics of chillers is also developed. The subprogram has stable and fast computational characteristics.
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  • Akio KONNO, Hiroshi IWAI, Motohiro SAITO, Hideo YOSHIDA
    2010 Volume 18 Issue 3 Pages 103-114
    Published: 2010
    Released: November 03, 2010
    JOURNALS FREE ACCESS
    A precise evaluation of the active reaction area in the electrodes is important to design an effective solid oxide fuel cell (SOFC). A scale analysis and 1-D numerical simulations are conducted to obtain a better understanding of the electrochemical reaction area in SOFC anode. In the scale analysis, the characteristic lengths of the electron, oxide ion and gas diffusions are evaluated from their conservation equations. Relative comparisons of the characteristic lengths show that the transport phenomena in the SOFC anode are primarily governed by the oxide ion conduction under standard operating conditions. The gas diffusion may affect the extent and the location of the active reaction area at high temperature and⁄or low reaction gas concentration conditions. 1-D numerical simulations for an anode provided detailed information such as the electron⁄ion potential distributions, the gas concentration distribution and local reaction rate. It is found that the electrochemical reaction actively occurs at the vicinity of the anode-electrolyte interface. The reaction thickness increases as the characteristic length of the ion conduction is increased resulting in a better power generation performance. The reaction thickness is also increased when the gas diffusion length is short. The cell performance is, however, lowered in this case because the low gas diffusivity yields the increase of the ohmic loss of ion conduction as well as the concentration overpotential.
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