ABSTRACT
Flow through packed beds of spheres is a complex phenomenon and it has been extensively studied. Although, there is many different correlations there is still no reliable universal equation for prediction of pressure drop. The paper presents the results of experimental research of pressure drop in packed bed of monosized spheres of three different diameters, 8, 11, and 13 mm set within cylindrical vessel of diameter dk = 74 mm, and two different heights of packed bed, hs = 300 and 400 mm. It has been proposed modification of widely used Ergun’s equation in the form of fp = [150+1.3•(Rep/(1-ε))]•(1-ε)2/(ε3×Rep) and new correlation fp = 1/[(27.4-25700•dh)/Rep+0.545+6.85•dh] for pressure drop calculation in simple and convenient form for hand and computer calculations. For total number of 362 experimental runs the correlation ratio of the modified Ergun’s relation was CR = 99.3%, and standard deviation SD = 12.2%, while novel relation has CR = 93.7% and SD = 5.4%. [Project of the Serbian Ministry of Education, Science and Technological Development, Grant no. 33049]
KEYWORDS
PAPER SUBMITTED: 2016-10-25
PAPER REVISED: 2016-11-25
PAPER ACCEPTED: 2016-12-19
PUBLISHED ONLINE: 2017-01-14
THERMAL SCIENCE YEAR
2017, VOLUME
21, ISSUE
Supplement 3, PAGES [S717 - S724]
- Stamenić, M.S., Research on working parameters of combustion the low calorific gaseous fuels and waste industrial gases in porous ceramic burner, Ph.D. thesis, University of Belgrade, Faculty of Mechanical Engineering, 2014
- Montillet, A., Akkari, E., Comiti, J., About a correlating equation for predicting pressure drops through packed beds of spheres in a large range of Reynolds numbers, Chemical Engineering and Processing, 46 (2007), pp. 329-333
- Pešić, R., et al., Pressure drop in packed bed of spherical particles at ambient and elevated air temperatures, Chem. ind. Chem. Eng. Q., 21 (2015), 3, pp. 419-427
- Ergun, S., Fluid flow through packed columns, Chemical Engineering Progress, 48 (1952), 2, pp. 89-94
- Erdim, E., Akgiray, Ö., Demir, I., A revisit of pressure drop-flow rate correlations for packed beds of spheres, Powder Technology, 283 (2015), pp. 488-504
- Stamenić, M.S. et al., Results of experimental research on parameters that determine stable operating limits of ceramic burner with packed bed of uniform spheres for combustion of low calorific gaseous fuels, Proceedings 3rd International Symposium on Environmental Friendly Energies and Applications, EFEA 2014, Paris, France, 2014, pp. 1-5
- Jaćimović, B., Genić, S., Froth Porosity and Clear Liquid Height in Trayed Columns, Chemical Engineering and Technology, 23 (2000), 2, pp. 171-176
- Genić, S., Jaćimović, B., Latinović, B., Research on air pressure drop in helically-finned tube heat exchangers, Applied Thermal Engineering, 26 (2006), 5-6, pp. 478-485
- Genić, S., Jaćimović, B., Janjić, B., Experimental research of highly viscous fluid cooling in cross-flow to a tube bundle, International Journal of Heat and Mass Transfer, 50 (2007), 7-8, pp. 1288-1294.
- Stephan, P., et al., VDI Heat Atlas, Spriger-Verlag, Berlin Heidelberg, Germany, 2010
- Lelea, D., The microtube heat sink with tangential impingement jet and variable fluid properties, Heat and Mass Transfer, 45 (2009), 9, pp. 1215-1222
- Mitrović, Z., Arandjelović, I., Existence of Generalized Best Approximations, Journal of nonlinear and convex analysis, 15 (2014), 4, pp. 787-792
- Salemović, D., Dedić, A., Ćuprić, N., A mathematical model and simulation of the drying process of thin layers of potatoes in a conveyor-belt dryer, Thermal Science 19 (2015), 3, pp. 1107-1118