Thermal Distribution in Axial-Flow Fixed Bed with Flowing Gas
Commenced in January 2007
Frequency: Monthly
Edition: International
Paper Count: 32794
Thermal Distribution in Axial-Flow Fixed Bed with Flowing Gas

Authors: Kun Lei, Hongfang Ma, Haitao Zhang, Weiyong Ying, Dingye Fang

Abstract:

This paper reported an experimental research of steady-state heat transfer behaviour of a gas flowing through a fixed bed under the different operating conditions. Studies had been carried out in a fixed-bed packed methanol synthesis catalyst percolated by air at appropriate flow rate. Both radial and axial direction temperature distribution had been investigated under the different operating conditions. The effects of operating conditions including the reactor inlet air temperature, the heating pipe temperature and the air flow rate on temperature distribution was investigated and the experimental results showed that a higher inlet air temperature was conducive to uniform temperature distribution in the fixed bed. A large temperature drop existed at the radial direction, and the temperature drop increased with the heating pipe temperature increasing under the experimental conditions; the temperature profile of the vicinity of the heating pipe was strongly affected by the heating pipe temperature. A higher air flow rate can improve the heat transfer in the fixed bed. Based on the thermal distribution, heat transfer models of the fixed bed could be established, and the characteristics of the temperature distribution in the fixed bed could be finely described, that had an important practical significance.

Keywords: Thermal distribution, heat transfer, axial-flow, fixed bed.

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1084396

Procedia APA BibTeX Chicago EndNote Harvard JSON MLA RIS XML ISO 690 PDF Downloads 2434

References:


[1] K. C. Xie, D. Y. Fang, Methanol technology, Beijing: Chemical Industry Press, 2010
[2] H. F. Ma, W. Y. Ying, D. Y Fang, "Simulation of a combined converter for methanol synthesis", Journal of east China University of Science and Technology, vol. 34, no. 2, pp. 149-153, 2008
[3] R. Caulkin, A. Ahmad, M. Fairweather, X. Jia, R. A. Williams, "An investigation of sphere packed shell-side columns using a digital packing algorithm". Computers and Chemical Engineering, vol. 31, no.12, pp. 1715-1724, December. 2007
[4] A Cybulski, J. A Moulijn, Structured catalysts and reactors, New York: Marcel Dekker Inc, 2th, pp. 1-18, 1998
[5] H. Freund, T. Zeiser, F. Huber, E. Klemm, G. Brenner, F. Durst, G. Emig, "Numerical simulations of single phase reacting flows in randomly packed fixed-bed reactors and experimental validation", Chemical Engineering Science, vol. 58, no. 3-6, pp. 903-910, February-March. 2003
[6] S. S. Bertsch, E. A. Groll, S. V. Garimella, "A composite heat transfer correlation for saturated flow boiling in small channels", International Journal of Heat and Mass Transfer, vol. 52, no7-8, pp. 2110-2118, March. 2009
[7] A. G. Dixon, G. Walls, H. Stanness, M. Nijemeisland, E. H. Stitt, "Experimental validation of high Reynolds number CFD simulations of heat transfer in a pilot-scale fixed bed tube", Chemical Engineering Journal, vol. 200-202, pp. 244-256, 15 August. 2012
[8] A. Guardo, M. Coussirat, F. Recasens, M. A. Larrayoz, X. Escaler, "CFD study on particle-to-fluid heat transfer in fixed bed reactors: Convective heat transfer at low and high pressure", Chemical Engineering Science, vol. 61, no. 13, pp. 4341-4353, July. 2006
[9] H. P. A. Calis, J. Nijenhuis, B. C. Paikert, F. M. Dautzenberg, C. M. van den Bleek, "CFD modelling and experimental validation of pressure drop and flow profile in a novel structured catalytic reactor packing", Chemical Engineering Science, vol. 56, no. 4, pp. 1713-1720, February. 2001
[10] J. Xu, W. S. Wei, A. Z. Tian, Y. Fan, X. J. Bao, C. C. Yu, "Temperature profile in a two-stage fixed bed reactor for catalytic partial oxidation of methane to syngas", Catalysis Today, vol. 149, no. 1-2, pp. 191-195, 15 January. 2010
[11] J. M. Wu, H. T. Zhang, W. Y. Ying, D. Y. Fang, "Thermal conductivity of cobalt-based catalyst for Fischer-Tropsch synthesis", International journal of thermophysics, vol. no. 3, pp. 556-571, March. 2010
[12] D. S. Wen, Y. L. Ding. "Heat transfer of gas flowthrough a packed bed", Chemical Engineering Science, vol. 61, no. 11, pp. 3532-3542, June. 2006
[13] Y. L. Ding, Z. L. Wang, D. S. Wen, M. Ghadiri, X. F. Fan, D. Parker, "Solids behaviour in a gas-solid two-phase mixture flowing through a packed particle bed", Chemical Engineering Science, vol. 60, no. 19, pp. 5231-5239, September. 2005
[14] C. A Coberly, W. R Marshall. "Temperature gradients in gas streams flowing through fixed granular beds", Chemical Engineering Progress, vol. 47, pp. 141-147, 1951
[15] A.P. de Wasch, G.F. Froment, "Heat transfer in packed beds", Chemical Engineering Science, vol. 27, no. 3, pp. 567-576, March. 1972
[16] A. G. Dixon, W. R. Paterson. "Heat transfer in packed beds of low tube/particle diameter Ratio", Houston: ACS Publications, pp. 238-253, 1978