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Modelling of heat transfer in a packed bed column

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The CFD modelling of heat transfer in the packed bed column in the laminar and turbulent fl ow regimes has been presented. Three numerical grids with different densities were generated for the packed bed column. The modelling was performed with the use of the Porous Media Model for treating the flow inside a porous structure. The standard k-ε model along with the logarithmic wall functions for the turbulent flow range was used. The infl uence of the mesh size on the accuracy of the fluid flow was studied. Both radial and axial direction temperature distributions have been compared with the experimental data1 and the values calculated from a 2DADPF model. A good agreement between the experimental and the predicted values of the pressure drop, temperature distributions and heat transfer coefficient was obtained.
Rocznik
Strony
34--41
Opis fizyczny
Bibliogr. 28 poz., rys., tab.
Twórcy
  • West Pomeranian University of Technology, Szczecin, Institute of Chemical Engineering and Environmental Protection Processes, al. Piastow 42, 71-065 Szczecin, Poland, Paulina.Pianko@zut.edu.pl
Bibliografia
  • 1. Wen, D. & Ding, Y. (2006). Heat transfer of gas flow through a packed bed. Chem. Eng. Sci. 61, 3532–3542. DOI: 10.1016/j.ces.2005.12.027.
  • 2. McGreavy, C., Foumeny, E.A. & Javed, K.H. (1986). Characterization of transport properties for fi xed bed in terms of local bed structure and fl ow distribution. Chem. Eng. Sci. 41, 787–797. DOI: 10.1016/0009-2509(86)87159-7.
  • 3. Stephenson, J.L. & Stewart, W.E. (1986). Optical measurements of porosity and fl uid motion in packed beds. Chem. Eng. Sci. 41, 2161–2170. DOI: 10.1016/0009-2509(86)87132-9.
  • 4. Kutsovsky, Y.E., Scriven, L.E., & Davis, H.T. (1196). NMR imaging of velocity profi les and velocity distribution in bead packs. Phys. Fluids. 8, 863–871. DOI: 10.1063/1.868867.
  • 5. Bey, O. & Eigenberger, G. (2001). Gas fl ow and heat transfer through catalyst fi lled tubes. Int. J. Therm. Sci. 40, 152–164. DOI: 10.1016/S1290-0729(00)01204-7.
  • 6. Collier, A., Hayhurst, A., Richardson, J. & Scott S. (2004). The heat transfer coeffi cient between particle and a bed (packed or fl uidised) of much larger particles. Chem. Eng. Sci. 59, 4613–4620. DOI: 10.1016/j.ces.2004.07.029.
  • 7. Calderbank, P. & Pogorski, L. (1957). Heat transfer In packed beds. Trans. Inst. Chem. Eng. 35, 195–207.
  • 8. Yagi, S. & Kunii, D. (1960). Studies on heat transfer near wall surfaces in packed beds. J. Amer. Inst. Chem. Eng. 1, 97–104.
  • 9. Li, C. & Finlayson, B. (1977). Velocity, temperature and conversion profi les in fi xed bed catalytic reactors. Chem. Eng. Sci. 32, 853–861. DOI: 10.1016/0009-2509(77)80071-7.
  • 10. Demirel, Y., Sharma, R. & Al-Ali, H. (2000). On the effectivefective heat transfer parameters in a packed bed. Int. J. Heat & Mass Tran. 43, 327–332. DOI: 10.1016/S0017-9310(99)00126-X.
  • 11. Yuen, E.H.L., Sederman, A.J., Sani, F., Alexander, P. & Gladden, L.F. (2003). Correlations between Local Conversion and Hydrodynamics in a 3-D Fixed-Bed Exterifi cation Process: An MRI and Lattice-Boltzmann Study. Chem. Eng. Sci. 58, 613–619. DOI: 10.1016/S0009-2509(02)00586-9.
  • 12. Sullivan, S.P., Sani, F.M., Johns, M.L. & Gladden, L.F. (2005). Simulation of Packed Bed Reactors Using Lattice Boltzmann Methods. Chem. Eng. Sci. 60, 3405–3418. DOI: 10.1016/j.ces.2005.01.038.
  • 13. Sørensen, J.P. & Stewart, W.E. (1974). Computation of Forced Convection in Slow Flow through Ducts and Packed Beds. Chem. Eng. Sci. 29 (3) 819–825. DOI: 10.1016/0009-2509(74)80200-9.
  • 14. Guardo, A., Coussirat, M., Larrayoz, M.A., Recasens, F. & Egusquiza, E. (2005). Infl uence of the Turbulence Model in CFD Modeling of Wall-to-Fluid Heat Transfer in Packed Beds. Chem. Eng. Sci. 60, 1733–1742. DOI: 10.1016/j.ces.2004.10.034.
  • 15. Dixon, A.G. & Nijemeisland, M. (2001). CFD as a Design Tool for Fixed-Bed Reactors. Ind. Eng. Chem. Res. 40, 5246–5254. DOI: 10.1021/ie001035a.
  • 16. Calis, H.P.A., Nijenhuis, J., Paikert, B.C., Dautzenberg, F.M. & van den Bleek, C.M. (2001). CFD Modelling and Experimental Validation of Pressure Drop and Flow Profile in a Novel Structured Catalytic Reactor Packing. Chem. Eng. Sci. 56, 1713–1720. DOI: S0009-2509(00)00400-0.
  • 17. Magnico, P. (2003). Hydrodynamic and Transport Properties of Packed Beds in Small Tube-to-Sphere Diameter Ratio: Pore Scale Simulation Using an Eulerian and a Langrangian Approach. Chem. Eng. Sci. 58, 5005–5024. DOI: 10.1016/S0009-2509(03)00282-3.
  • 18. Romkes, S.J.P., Dautzenberg, F.M., van den Bleek, C.M. & Calis, H.P.A. (2003). CFD Modelling and Experimental Validation of Particle-to-Fluid Mass and Heat Transfer in a Packed Bed at Very Low Channel-to-Particle Diameter Ratio. Chem. Eng. J. 96, 3–13. DOI: 10.1016/j.cej.2003.08.026.
  • 19. Logtenberg, S. & Dixon, A. (1998). Computational fluid dynamics studies of fi xed bed heat transfer. Chem. Eng. Proc. 37, 7–21. DOI: 10.1016/S0255-2701(97)00032-9.
  • 20. Dixon, A.G. & van Dongeren, J.H. (1998). The influence of the tube and particle diameters at constant ration on heat transfer in packed beds. Chem. Eng. Proc. 37, 23–32. DOI: S0255-2701(97)00033-0.
  • 21. ANSYS Fluent 12.0/12.1 Documentation, 2010.
  • 22. Peters, S.T. (1998). Handbook of composites. Springer-Verlag.
  • 23. Ergun, S. (1952). Fluid fl ow through packed columns. Chem. Eng. Prog. 48, 89–94.
  • 24. Macdonald, I.F., El-Sayed, M.S., Mow, K. & Dullien, F.A.L. (1979). Flow through porous media - the Ergun equation revisited. Ind. Eng. Chem. Fundam. 18(3), 199–208. DOI: 10.1021/i160071a001.
  • 25. Mueller, G.E. (2010). Radial porosity in packed beds of spheres. Powd. Tech. 203, 626–633. DOI: 10.1016/j.powtec.2010.07.007.
  • 26. Nijemeisland, M. & Dixon, A.G. (2001). Comparison of CFD simulations to experiment for convective heat transfer in a gas-solid fi xed bed. Chem. Eng. J. 82, 231–246. DOI: 10.1016/S1385-8947(00)00360-0.
  • 27. Freiwald, M.G. & Paterson, W.R. (1992). Accuracy of model predictions and reliability of experimental data for heat transfer in packed beds. Chem. Eng. Sci. 47, 1545–1560. DOI: 10.1016/0009-2509(92)85003-T.
  • 28. Ding, Y.L., Wang, Z.L., Wen, D.S., Ghadiri, M., Fan, X.F. & Parker, D.J. (2005). Solids behaviour in a gas-solid two-phase mixture fl owing through a packed particle bed. Chem. Eng. Sci. 60, 5231–5239. DOI: 10.1016/j.ces.2005.04.052.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPS3-0021-0082
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