Local instantaneous temperature signal and time-averaged heat transfer coefficient were measured using a miniature heat transfer probe. The experiments were carried out in the bottom zone of a 5.8 m high, 0.3 m Γ 0.5 m rectangular cross-section circulating fluidized bed. The results show that the he
Method of calculation of heat transfer coefficient of the heater in a circulating fluidized bed furnace
β Scribed by J.F. Lu; J.S. Zhang; G.X. Yue; Q. Liu; L. Yu; X.D. Lin; W.J. Li; Y. Tang; T.Y. Luo; R.S. Ge
- Publisher
- John Wiley and Sons
- Year
- 2002
- Tongue
- English
- Weight
- 365 KB
- Volume
- 31
- Category
- Article
- ISSN
- 1099-2871
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β¦ Synopsis
Abstract
Knowledge of heat transfer coefficients is important in the design and operation of CFB boilers. It is the key to determining the area and the layout of the heat transfer surfaces in a CFB furnace. Local bulk density has a close relationship to the local heat transfer coefficient. Using a heat flux probe and bulk density sampling probe, the local bed to wall heat transfer coefficient in the furnace of a 75 t/h CFB boiler was measured. According to the experimental results and theoretical analysis of the facts that influence the heat transfer, the heat transfer coefficient calculation method for the CFB furnace was developed. The heat transfer surface configuration, heating condition, and the material density are considered in this method. The calculation method has been used in the design of CFB boilers with a capacity from 130 t/h to 420 t/h. Β© 2002 Wiley Periodicals, Inc. Heat Trans Asian Res, 31(7): 540β550, 2002; Published online in Wiley InterScience (www.interscience.wiley.com). DOI 10.1002/htj.10056
π SIMILAR VOLUMES
The characteristics of heat transfer were studied in both a gas-solids concurrent downflow fluidized bed (downer) and a gassolids concurrent upflow fluidized bed (riser) with FCC particles. The radial and axial distribution profiles of the heat transfer coefficient between a suspended surface and th