Abstract
Using the external heat exchanger in large-scale CFB boilers can control combustion and heat transfer separately, make the adjustments of bed temperature and steam temperature convenient. The state of gas-solid two phase flow in the external heat exchanger is bubbling fluidized bed, but differs from the regular one as there is a directional flow in it. Consequently, the temperature distribution changes along the flow direction. In order to study the heat transfer characteristics of the water cooled tubes in the bubbling fluidized bed and ensure the uniformity of heat transfer in the external heat exchanger, a physical model was set up according to the similarity principle and at the geometric ratio of 1∶28 to an external heat exchanger of a 300MW CFB boiler. The model was connected with an electrically heated CFB test-bed which provides the circulating particles. The influencing factors and the distribution rule of the particles’ heat transfer coefficient in the external heat exchanger were assessed by measuring the temperature changes of the water in the tubes and different parts of particles flow along the flow direction. At the end, an empirical correlation of particles’ heat transfer coefficient in external heat exchanger was given by modifying the Veedendery empirical correlation.
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© 2009 Tsinghua University Press, Beijing and Springer-Verlag Berlin Heidelberg
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Ji, X.Y., Lu, X.F., Yang, L., Liu, H.Z. (2009). The Experimental Study on Heat Transfer Characteristics of The External Heat Exchanger. In: Yue, G., Zhang, H., Zhao, C., Luo, Z. (eds) Proceedings of the 20th International Conference on Fluidized Bed Combustion. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-02682-9_55
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DOI: https://doi.org/10.1007/978-3-642-02682-9_55
Publisher Name: Springer, Berlin, Heidelberg
Print ISBN: 978-3-642-02681-2
Online ISBN: 978-3-642-02682-9
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