TY - JOUR
T1 - Heat Transfer and Pressure loss of a very shallow fluidized-bed heat exchanger Part 1. Experiment with a single row of tubes
AU - Aihara, Toshio
AU - Maruyama, Shigenao
AU - Hongoh, Mitsuo
AU - Aya, Sunao
N1 - Funding Information:
We wish to express our thanks to Professor A. Sugawara for his measurement of the specific heat and density of the glass beads. The research was carried out partly with the grants-in-aid B-604~107 for scientific research and 61850035 for developmental scientific research of the Ministry of Education, Science and Culture of Japan, and by using a part of the experimental facilities for heat transfer of multiphase flow \[19, 20\] in the Institute.
PY - 1988/10
Y1 - 1988/10
N2 - A novel gas fluidized-bed heat exchanger with a very small static bed height has been developed for a heat-exchanging system using a low-pressure fan. This fluidized bed is composed of a multislit distributor, a single row of 8 mm diameter tubes, and glass beads 48-195 μm in diameter. The measured performance of heat transfer is excellent and that of fluidization is satisfactory, in spite of the static bed height being as small as 13 mm. In the best case, the test fluidized bed exhibited a heat transfer performance comparable to that of a conventional fluidized bed with a perforated plate distributor and a static bed height of 150 mm, and showed one-fourteenth the pressure loss.
AB - A novel gas fluidized-bed heat exchanger with a very small static bed height has been developed for a heat-exchanging system using a low-pressure fan. This fluidized bed is composed of a multislit distributor, a single row of 8 mm diameter tubes, and glass beads 48-195 μm in diameter. The measured performance of heat transfer is excellent and that of fluidization is satisfactory, in spite of the static bed height being as small as 13 mm. In the best case, the test fluidized bed exhibited a heat transfer performance comparable to that of a conventional fluidized bed with a perforated plate distributor and a static bed height of 150 mm, and showed one-fourteenth the pressure loss.
KW - convective heat transfer
KW - fluidized bed
KW - heat exchanger
KW - multiphase flow
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U2 - 10.1016/0894-1777(88)90012-X
DO - 10.1016/0894-1777(88)90012-X
M3 - Article
AN - SCOPUS:0024101646
SN - 0894-1777
VL - 1
SP - 315
EP - 323
JO - Experimental Thermal and Fluid Science
JF - Experimental Thermal and Fluid Science
IS - 4
ER -