Heat and Mass Transfer and Volume Variations during Drying of Industrial Ceramic Bricks: An Experimental Investigation

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The purpose of this paper is to present an experimental study of brick drying. For the drying experiments, industrial brick (clay) was dried in an oven under controlled conditions of air velocity, air temperature and air relative humidity. The continuous drying experiments ended when the mass reached constant weight. In order, to obtain the balanced moisture content, each sample was kept under the same drying air temperature for 48 hours inside the oven. The tests were performed under atmospheric pressure. Results of the drying and heating kinetics and volume variations during the process are shown and analyzed. It was verified that air temperature has big influence in the drying rate during process. It was verified that the largest temperature, moisture content and stress gradients are located in the vertexes of the brick. The drying process happens in the falling drying rate period.

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Defect and Diffusion Forum (Volumes 326-328)

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267-272

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April 2012

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] W.D. Callister, Jr. and D.G. Rethwisch: Fundamentals of materials science and engineering: an integrated approach (3rd. ed. John Wiley & Sons, Inc. USA, 2008).

Google Scholar

[1] W.D. Callister, Jr.: Materials science and engineering. An introduction (7rd ed., John Wiley & Sons, Inc. USA, 2007).

Google Scholar

[3] D.A. Brosnan and G.C. Robinson: Introduction of drying of ceramics: with laboratory exercises (The American Ceramic Society Westerville, 2003).

Google Scholar

[4] M. Hasatani and Y. Itaya: Drying'96 Vol. A (1996), p.27.

Google Scholar

[5] Y. Itaya and M. Hasatani: Drying Technol. Vol. 14 (1996), p.1301.

Google Scholar

[6] J.S. Reed: Principles of ceramics processing (John Wiley & Sons, Inc., New York, 1995).

Google Scholar

[7] A. Sander, D. Skanki and B. Nenad: Ceramics Int. Vol. 29 (2003), p.641.

Google Scholar

[8] A.A.J. Ketelaars, W. Jomaa, J.R. Puiggali and W.J. Coumans: Drying'92 Vol. A (1992), p.293.

Google Scholar

[9] A.J.J. van der Zanden, A.M.E. Schoenmakers and P.J.A.M. Kerkof: Drying Technol. Vol. 14 (1996), p.647.

Google Scholar

[10] S. Su: Applied Clay Sci. Vol. 12 (1997), p.189.

Google Scholar

[11] A.J.J. van der Zanden: Modelling and simulating simultaneous liquid and vapour transport in partially saturated porous materials (in: Mathematical Modeling and Numerical Techniques in Drying Technology, New York: Marcel Dekker, Inc., 1997).

Google Scholar

[12] Y. Itaya, S. Taniguchi and M. Hasatani: Drying Technol. Vol 15, no. 1 (1997), p.1.

Google Scholar

[13] Y. Itaya, S. Mori and M. Hasatani: Drying'98 Vol. A (1998), p.240.

Google Scholar

[14] G. Musielak: Drying'2000 Vol. 1 (2000), p.1.

Google Scholar

[15] F. Augier, W.J. Coumans, A. Hugget and E.F. Kaasschieter: Chem. Eng. J. Vol. 86 (2002), p.133.

Google Scholar

[16] J. Banaszak and S. Kowalski: Drying'2000 Vol. 1 (2000), p.1.

Google Scholar

[17] B. Kroes, W.J. Coumans and P.J.A.M. Kerkhof: Drying'96 Vol. A (1996), p.159.

Google Scholar

[18] J.B. Silva: Ph. Thesis, Federal University of Campina Grande, Campina Grande, Brazil, (2009).

DOI: 10.21475/ajcs.18.12.08.pne1177

Google Scholar

[19] J.B. Silva, G.S. Almeida, W.C.P. B. de Lima, G.A. Neves and A.G.B. de Lima: Def. Diff. Forum Vols. 312-315 (2011), p.971.

Google Scholar