Abstract
In this paper, we apply a novel immersed boundary method to simulate pore-scale level fluid flow and convective heat transfer in realistic numerically generated open-cell solid foams in a Cartesian computational domain. Five different periodic foam samples of varying porosities (ε=[0.877,0.948]) are generated by numerically mimicking the actual foam formation process (minimizing surface area). The step-by-step procedure for generating the periodic foam geometries is presented. The specific surface areas of the generated foams of different porosities are compared with real foam geometries showing a reasonable agreement. The Reynolds number (Re) is varied from Re≈0 (creeping flow) to Re≈500, and finally drag and Nusselt correlations have been proposed. A detailed analysis is presented on the local velocity and temperature field for the fluid-solid interaction in a complex cellular porous medium.
Original language | English |
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Pages (from-to) | 260-274 |
Number of pages | 15 |
Journal | Chemical Engineering Science |
Volume | 183 |
DOIs | |
Publication status | Published - 29 Jun 2018 |
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Keywords
- Cellular porous media
- Drag closure
- Heat transfer closure
- Immersed boundary method
- Open-cell solid foams
- Periodic boundary treatment
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Drag and heat transfer closures for realistic numerically generated random open-cell solid foams using an immersed boundary method. / Das, S.; Sneijders, S.; Deen, N.G.; Kuipers, J.A.M.
In: Chemical Engineering Science, Vol. 183, 29.06.2018, p. 260-274.Research output: Contribution to journal › Article › Academic › peer-review
TY - JOUR
T1 - Drag and heat transfer closures for realistic numerically generated random open-cell solid foams using an immersed boundary method
AU - Das, S.
AU - Sneijders, S.
AU - Deen, N.G.
AU - Kuipers, J.A.M.
PY - 2018/6/29
Y1 - 2018/6/29
N2 - In this paper, we apply a novel immersed boundary method to simulate pore-scale level fluid flow and convective heat transfer in realistic numerically generated open-cell solid foams in a Cartesian computational domain. Five different periodic foam samples of varying porosities (ε=[0.877,0.948]) are generated by numerically mimicking the actual foam formation process (minimizing surface area). The step-by-step procedure for generating the periodic foam geometries is presented. The specific surface areas of the generated foams of different porosities are compared with real foam geometries showing a reasonable agreement. The Reynolds number (Re) is varied from Re≈0 (creeping flow) to Re≈500, and finally drag and Nusselt correlations have been proposed. A detailed analysis is presented on the local velocity and temperature field for the fluid-solid interaction in a complex cellular porous medium.
AB - In this paper, we apply a novel immersed boundary method to simulate pore-scale level fluid flow and convective heat transfer in realistic numerically generated open-cell solid foams in a Cartesian computational domain. Five different periodic foam samples of varying porosities (ε=[0.877,0.948]) are generated by numerically mimicking the actual foam formation process (minimizing surface area). The step-by-step procedure for generating the periodic foam geometries is presented. The specific surface areas of the generated foams of different porosities are compared with real foam geometries showing a reasonable agreement. The Reynolds number (Re) is varied from Re≈0 (creeping flow) to Re≈500, and finally drag and Nusselt correlations have been proposed. A detailed analysis is presented on the local velocity and temperature field for the fluid-solid interaction in a complex cellular porous medium.
KW - Cellular porous media
KW - Drag closure
KW - Heat transfer closure
KW - Immersed boundary method
KW - Open-cell solid foams
KW - Periodic boundary treatment
UR - http://www.scopus.com/inward/record.url?scp=85044112454&partnerID=8YFLogxK
U2 - 10.1016/j.ces.2018.03.022
DO - 10.1016/j.ces.2018.03.022
M3 - Article
AN - SCOPUS:85044112454
VL - 183
SP - 260
EP - 274
JO - Chemical Engineering Science
JF - Chemical Engineering Science
SN - 0009-2509
ER -