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

  • Mohammed A. Atiya Biochem.Eng.Dept.,Al-khwarizmi Coll.Eng Baghdad University
  • Fadhil S. Kadhim Biochem.Eng.Dept.,Al-khwarizmi Coll.Eng Baghdad University


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.


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(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.
How to Cite
Atiya, M., & Kadhim, F. (2008). Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant. Al-Khwarizmi Engineering Journal, 4(1), 1-7. Retrieved from