Heat transfer from a grid jet in a large fluidized bed
作者:
L. A. Behie,
M. A. Bergougnou,
C. G. J. Baker,
期刊:
The Canadian Journal of Chemical Engineering
(WILEY Available online 1975)
卷期:
Volume 53,
issue 1
页码: 25-30
ISSN:0008-4034
年代: 1975
DOI:10.1002/cjce.5450530104
出版商: Wiley Subscription Services, Inc., A Wiley Company
数据来源: WILEY
摘要:
AbstractHeat transfer from a vertical grid jet within a 2 ft diameter and 4 ft deep fluidized bed of cracking catalyst was studied. The test nozzle diameter was varied from ¼ to 1 in. and the nozzle velocity from 50 to 250 ft /sec which is within the range of industrial practice. The axial temperature data have been related to a Froude, a Reynolds and a Nozzle number:In (δT/δTo) = –58.1 Fr−0.562No1.08Re−0.112A simple jet quenching model yielded heat transfer coefficients between the fluid bed and grid jet which ranged from 300 to 1200 Btu/
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