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Experimental Study of Factors Affecting Corrosion in Gas Wells Using Potantio Acetate and Galvan Acetate Tests

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Abstract (2. Language): 
Further deterioration in gas wells due to localized corrosion occurs. The local corrosion under the insulation, the deposits or to be caused by bacteria, 10 to 100 times faster than the corrosion damage is uniform. CO2 corrosion in gas wells temperature can be divided into three regions: A) Temperature below 140 degrees Fahrenheit (C60) does not protect the product and the level of corrosion caused by severe corrosion exists. B) Above 300 degrees F (C150), Mgntayt is formed and the environment unless the presence of large amounts of salt water, is slightly corrosive. C) Between 300-140 degrees Fahrenheit (C150 -60) has the ability to protect the metal carbonate product layer does not even need a deterrent. But in the presence of ions such as chloride or hydrogen sulfide, or the destructive effect of high velocity fluid layer may be destroyed. Circumstances of high-speed m / s 10 and turbulent fluid flow, creating a protective layer, it is unstable. Scientists Believes that the growth of iron carbonates (FeCO3) crystals incomplete causes a small anodic area and the wounded are yellow corrosion, at temperatures above C100 product of pyrite (FeS2) was created on the metal surface is quite stable in terms of thermodynamic. At lower temperatures the formation of this layer decreases and the corrosion rate increases. Corrosion is usually lower than the concentration in ppm 2000 in the sour wells gas in the range pH 5 to 5 / 6 occurs. In this article discussed about laboratory factors affecting corrosion in gas wells using Potantio acetate and Galvano acetate and Potantio dynamics tests.
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REFERENCES

References: 

[1] Mars. C. Fontana: Corrosion Engineering, translated by A. Saatchi, Journal of Isfahan University Jihad, Third Edition Autumn 2001
[2] Saif, Siamak, karami nori. Hussein: an analysis of the interaction of stray currents, Persian date Khordad 1378
[3] D.. L. Pyron; corrosion electrochemistry; translation Golazar MA; Isfahan; Isfahan University Press, 1999
[4] Samimi, Amir. Zarinabadi, Soroush. Water penetration in the three-layer poly ethylene coating, Europe Congress of Chemical Engineering, 2010
[5] T.C. Chevro, M. Bonis, "Use of pH Stablization of Corrosion Control of Long Multiphase Pipelines", TOTAL FINA ELF, second congress of corrosion in oil Industries , Iran , Oil Industry University
[6] Zarinabadi, Soroush, Samimi, Amir," Problems of hydrate formation in oil and gas pipes deal," Australian journal of basic and applied science, 2011
[7] Samimi, Amir, Zarinabadi, Soroush, "Reduction of greenhouse gases emission and effect on environment.", Australian journal of basic and applied science, 752-756, 2011
[8] Samimi, Amir, Zarinabadi, Soroush," an Analysis of Polyethylene Coating Corrosion in Oil and Gas Pipelines," Journal of American science, U.S.A., 2011
[9] Zarinabadi, Soroush, Samimi, Amir," Scrutiny Water Penetration in Three-layer Polyethylene Coverage", Journal of American science, U.S.A., 2011

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