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G9 Fluid-Particle Heat Transfer in Flow Through Packed Beds of Solids

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VDI Heat Atlas

Part of the book series: VDI-Buch ((VDI-BUCH))

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

$$\dot q = \alpha \;\rm \Delta T _{{\rm{LM}}}$$

The logarithmic mean temperature difference is given by

$$\rm \Delta T _{{\rm{L}}{\rm{M}}} = {{(T _{\rm{w}} -T...

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5 Bibliography

  1. 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

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  3. 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

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  4. Schlünder EU (1976) Über den Mechanismus der Stoffübertragung in Kontaktapparaten. Verfahrenstechnik 10(10):645–650

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  5. 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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© 2010 Springer-Verlag

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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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