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           by rapid oxidation. This thick oxide scale was usually cracked because the heat expansion coefficient
            of the oxide was different from that of the tube metal on which the scale is attached. Through the
            opening of the oxide crack, fresh tube metal which was located beneath the oxide crack tip suffered
            repeated  oxidation  resulting in  small cracks initiating in  the  tube  metal.  Tube  failure finally
            occurred as a result of propagation of these small cracks to the outer surface of the tube. The
            failure could be prevented by maintaining the temperature of the tube at the flame side of the
            burner, that is, in the vicinity of supporting guide A in Fig. 1, below  1000°C by improving the
            existing combustion system or by modifying the burner tips.


            Acknowledgements

              The authors are grateful for the support provided by a grant from the KOSEF (Korea Science
            and Engineering Foundation) through  Safety and Structural Integrity Research Center in Sung
            Kyun Kwan University. The authors also would like to thank POSCO (Pohang Iron and Steel
            Co.) for providing samples.



            References

            [I]  Williamson J,  Shipley M. Life assessment and monitoring of furnace heaters, improving reliability in petroleum
              refineries and chemical and natural gas plants. Houston, TX, USA, Novembcr 9-12,  1992.
            [2]  Walter M, Schutze M, Rahmel A. Oxidation of Metals, 1993;40:37.
            [3] Life prediction of tubes for steam reformer and cracker. Document for Information Document No. 85, KHK, 1983.
            [4] Lai GY. High temperature corrosion of engineering alloy, ASM International, 1990.
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