Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant
pdf

How to Cite

Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant. (2008). Al-Khwarizmi Engineering Journal, 4(1), 1-7. https://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/526

Abstract

The electrochemical behavior of carbon steel in water sweetening station in Libya has been studied in the range of ( 293–333 oC) using weight loss technique. Measurements were carried out over a range of Reynolds number (5000 – 25000).An apparatus was designed for studying the corrosion process in the turbulent regime, which is of industrial significance. It was found that The corrosion rate of carbon steel in water sweetening station is under diffusion control and increases with increasing Reynolds number. On the other hand the variation of corrosion rate with temperature in the range of (293–333 oC) was found to follow Arrhenius equation and the activation energy approximately the same except at low Reynolds number.

pdf

References

(1) Uhlig, H.H ”Corrosion and corrosion control” Jhon Wiliey and Sons Inc., 2ndedition, 1977.
(2) Steiger wald, R,F, Corrosion J., 24, Jan., 1, 1968.
(3) Eckert, E.R, Introduction to the transfer of heat and mass, McGraw Hill, New York, 1950.
(4) Wormwell, F., J. Iron steel Ins., Vol.154, P.219, 1946.
(5) Speller, F.N. and Kendall, V.V., Ind. Eng. Chem. J., Vol.15, P.134, 1956.
(6) Cox, G.L.and Roetheli, B.E., Ind. Eng. Chem., Vol. 23, P.1012, 1931.
(7) West, J.M., Basic corrosion and oxidation, Eliss Horwood Ltd., west Sussex, P.40, 1980.
(8) Proter, D.T., Donnimirska, M. and Wall, R., Corrosion Sci, Vol.8, P.833, 1968.
(9) Shoulikidis, N., Vassiliou, P.G., Corrosion J., Vol.17, No.3, P.142, 1982.
(10) Francis, P.E., and Dolphin, A.S., Br. Corrosion J., Vol.19, No.4, P.181, 1984.
(11) Barnarts, S, Electrochemical Techniques for corrosion, 2nd, Printing, NACA, 1978.
(12) Champion, F.A., Corrosion testing procedure, 2nd edition, London, champion and Hill, 1964.
(13) Fadhil,S,Kadihim,M.Sc.,Thesis”Investigation of carbon steel corrosion under two phase and Multi- phase flow in horizontal pipes”, Petroleum Eng. Dept.,College of Engineering, University of Baghdad, 1996.
(14) Postlethwaite, J. and Hurp, D.R., Corrosion Sci, Vol. 7, P.435, 1976.
(15) Postlethwaite , J. and Hurp, D.R., Corrosion Sci, Vol. 7, P435, 1967.
(16) Chin, R.G. , and Nobe, K., Corrosion J. Vol. 23 , P. 364 , 1977.
(17) Chin R.J., and Nobe, K, N.M. and Hakerman, N., J.Electrochem. Soc., Vol. 102, P. 333, 1955.
(18) Parshin, A.G., Pakhmov, V.S., and Kolotyrkin, YA.M. Corrosion Sci., Vol. 22, No.9, P. 845,1982.
(19) Atiya, M.A., Ph.D. Thesis, Dept. of Chem. Eng., University of Baghdad, Baghdad, 1996.
(20) Ross, T.K.and Hitchen, B.P., Corrosion Sci., 1, 65, 1961.

Copyright: Open Access authors retain the copyrights of their papers, and all open access articles are distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution and reproduction in any medium, provided that the original work is properly cited. The use of general descriptive names, trade names, trademarks, and so forth in this publication, even if not specifically identified, does not imply that these names are not protected by the relevant laws and regulations. While the advice and information in this journal are believed to be true and accurate on the date of its going to press, neither the authors, the editors, nor the publisher can accept any legal responsibility for any errors or omissions that may be made. The publisher makes no warranty, express or implied, with respect to the material contained herein.