Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant
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...
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Al-Khwarizmi College of Engineering – University of Baghdad
2008
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oai:doaj.org-article:55e6d4193a554d708ca954ae1529c27c2021-12-02T07:22:42ZCorrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant1818-11712312-0789https://doaj.org/article/55e6d4193a554d708ca954ae1529c27c2008-03-01T00:00:00Zhttp://alkej.uobaghdad.edu.iq/index.php/alkej/article/view/526https://doaj.org/toc/1818-1171https://doaj.org/toc/2312-0789 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. Mohammed A. AtiyaFadhil S. KadhimAl-Khwarizmi College of Engineering – University of BaghdadarticleChemical engineeringTP155-156Engineering (General). Civil engineering (General)TA1-2040ENAl-Khawarizmi Engineering Journal, Vol 4, Iss 1 (2008) |
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Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 |
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Chemical engineering TP155-156 Engineering (General). Civil engineering (General) TA1-2040 Mohammed A. Atiya Fadhil S. Kadhim Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant |
description |
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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format |
article |
author |
Mohammed A. Atiya Fadhil S. Kadhim |
author_facet |
Mohammed A. Atiya Fadhil S. Kadhim |
author_sort |
Mohammed A. Atiya |
title |
Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant |
title_short |
Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant |
title_full |
Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant |
title_fullStr |
Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant |
title_full_unstemmed |
Corrosion of Carbon Steel Pipeline in Flow System of water Sweetening Plant |
title_sort |
corrosion of carbon steel pipeline in flow system of water sweetening plant |
publisher |
Al-Khwarizmi College of Engineering – University of Baghdad |
publishDate |
2008 |
url |
https://doaj.org/article/55e6d4193a554d708ca954ae1529c27c |
work_keys_str_mv |
AT mohammedaatiya corrosionofcarbonsteelpipelineinflowsystemofwatersweeteningplant AT fadhilskadhim corrosionofcarbonsteelpipelineinflowsystemofwatersweeteningplant |
_version_ |
1718399456736444416 |