1 Introduction
Heat transfer coefficients between particles and fluid in packed beds are one of the basic pieces of information needed for unit operations and chemical reactor design. Heat transfer is of interest, for example, in chemical reactors with fixed beds of catalysts in which large amounts of heat are absorbed or released, or in fixed beds used as regenerative heat exchangers. Particles of very different shapes, such as spheres, cylinders, Raschig rings or Berl saddles are used as packing material. Chap. G9 deals with the calculation of heat transfer coefficients between a fluid flowing through a packed bed and the particles of the packed bed.
2 Definition of the Heat Transfer Coefficient
The average coefficient of heat transfer between the solid particles in a bed and a fluid flowing through the bed is defined by
The logarithmic mean temperature difference is given by
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5 Bibliography
Gnielinski V (1981) Equations for the calculation of heat and mass transfer during flow through stationary spherical packings at moderate and high Peclet numbers. Int Chem Eng 21(3):378–383
Gnielinski V (1982) Berechnung des Wärme- und Stoffaustauschs in durchstömten ruhenden Schüttungen. Verfahrenstechnik 16(1):36–39
Kunii D, Suzuki M (1967) Particle –to-fluid heat and mass transfer in packed beds of fine particles. Int J Heat Mass Transfer 10:840–852
Schlünder EU (1976) Über den Mechanismus der Stoffübertragung in Kontaktapparaten. Verfahrenstechnik 10(10):645–650
Martin H (1978) Low Peclet number particle-to fluid heat and mass transfer in packed beds. Chem Engn Sci 33:913–919
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Gnielinski, V. (2010). G9 Fluid-Particle Heat Transfer in Flow Through Packed Beds of Solids. In: VDI Heat Atlas. VDI-Buch. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-540-77877-6_42
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