This paper surveyed the most important, well known two-phase mass transfer models, namely film-, film-penetration- and surface renewal models, applying them to describe the three-phase mass transfer rates at the gas-liquid interface. These models should enable the user to predict the mass transfer enhancement in the presence of a third, in the mass transport active, dispersed phase. Depending on the particle size of the dispersed phase, the pseudo-homogeneous and/or the heterogeneous model can be recommended for nanometer sized and micrometer sized particles, respectively. The effect of all important mass transport parameters, namely particle size, surface renewal frequency, diffusion depth, solubility coefficient, has been shown by typical figures. It has been analyzed how strongly depends the applicability of the homogeneous- or the heterogeneous models not only on the particle size but on the mass transport parameters. As case study, the measured and the predicted mass transfer rates have been investigated in nanofluids.
| Published in | American Journal of Chemical Engineering (Volume 1, Issue 1) |
| DOI | 10.11648/j.ajche.20130101.15 |
| Page(s) | 24-35 |
| Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
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Copyright © The Author(s), 2013. Published by Science Publishing Group |
Three-Phase Mass Transport, Heterogeneous Model, Homogeneous Model, Nanoparticles
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APA Style
Endre Nagy, Krishna D. P. Nigam. (2013). Three-Phase Mass Transfer: Application of the Pseudo-Homogeneous and Heterogeneous Models. American Journal of Chemical Engineering, 1(1), 24-35. https://doi.org/10.11648/j.ajche.20130101.15
ACS Style
Endre Nagy; Krishna D. P. Nigam. Three-Phase Mass Transfer: Application of the Pseudo-Homogeneous and Heterogeneous Models. Am. J. Chem. Eng. 2013, 1(1), 24-35. doi: 10.11648/j.ajche.20130101.15
AMA Style
Endre Nagy, Krishna D. P. Nigam. Three-Phase Mass Transfer: Application of the Pseudo-Homogeneous and Heterogeneous Models. Am J Chem Eng. 2013;1(1):24-35. doi: 10.11648/j.ajche.20130101.15
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Download@article{10.11648/j.ajche.20130101.15,
author = {Endre Nagy and Krishna D. P. Nigam},
title = {Three-Phase Mass Transfer: Application of the Pseudo-Homogeneous and Heterogeneous Models},
journal = {American Journal of Chemical Engineering},
volume = {1},
number = {1},
pages = {24-35},
doi = {10.11648/j.ajche.20130101.15},
url = {https://doi.org/10.11648/j.ajche.20130101.15},
eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20130101.15},
abstract = {This paper surveyed the most important, well known two-phase mass transfer models, namely film-, film-penetration- and surface renewal models, applying them to describe the three-phase mass transfer rates at the gas-liquid interface. These models should enable the user to predict the mass transfer enhancement in the presence of a third, in the mass transport active, dispersed phase. Depending on the particle size of the dispersed phase, the pseudo-homogeneous and/or the heterogeneous model can be recommended for nanometer sized and micrometer sized particles, respectively. The effect of all important mass transport parameters, namely particle size, surface renewal frequency, diffusion depth, solubility coefficient, has been shown by typical figures. It has been analyzed how strongly depends the applicability of the homogeneous- or the heterogeneous models not only on the particle size but on the mass transport parameters. As case study, the measured and the predicted mass transfer rates have been investigated in nanofluids.},
year = {2013}
}
TY - JOUR T1 - Three-Phase Mass Transfer: Application of the Pseudo-Homogeneous and Heterogeneous Models AU - Endre Nagy AU - Krishna D. P. Nigam Y1 - 2013/06/30 PY - 2013 N1 - https://doi.org/10.11648/j.ajche.20130101.15 DO - 10.11648/j.ajche.20130101.15 T2 - American Journal of Chemical Engineering JF - American Journal of Chemical Engineering JO - American Journal of Chemical Engineering SP - 24 EP - 35 PB - Science Publishing Group SN - 2330-8613 UR - https://doi.org/10.11648/j.ajche.20130101.15 AB - This paper surveyed the most important, well known two-phase mass transfer models, namely film-, film-penetration- and surface renewal models, applying them to describe the three-phase mass transfer rates at the gas-liquid interface. These models should enable the user to predict the mass transfer enhancement in the presence of a third, in the mass transport active, dispersed phase. Depending on the particle size of the dispersed phase, the pseudo-homogeneous and/or the heterogeneous model can be recommended for nanometer sized and micrometer sized particles, respectively. The effect of all important mass transport parameters, namely particle size, surface renewal frequency, diffusion depth, solubility coefficient, has been shown by typical figures. It has been analyzed how strongly depends the applicability of the homogeneous- or the heterogeneous models not only on the particle size but on the mass transport parameters. As case study, the measured and the predicted mass transfer rates have been investigated in nanofluids. VL - 1 IS - 1 ER -
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