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Product Number:
51300-07565-SG
ISBN:
07565 2007 CP
Author:
J. D. Jong, A. Saunders-Tack, M. Sargent, A. M. Etheridge, W. C. Fort, and N. Dowling
Publication Date:
2007
$20.00
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Product Number:
51300-11120-SG
ISBN:
2011 11120 CP
Author:
Joseph Boivin and Scott Oliphant
Publication Date:
2011
$20.00
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Product Number:
51318-11320-SG
Author:
Saleh Al-Sulaiman / Sundip Kuthe / Sharad Londhe / Abdul Razzaq Al-Shamari
Publication Date:
2018
$20.00
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Product Number:
ED22-17120-SG
Author:
George Young, Jake Quincey, Andrew Brittan, Pit Shulze, Stella Tsotsos, Lars Parrington, Josef Parrington, Anne Demma, Micah Hackett, Samuel Briggs and Julie D. Tucker
Publication Date:
2022
$20.00
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Product Number:
51324-20853-SG
Author:
Ruqaia Al Rusheidi; Mohamed Ossama; Arwa Al Wahaibi; Talal Al Nabhani; Zaher Al Hajri
Publication Date:
2024
$40.00
The deposition of elemental sulfur is a major concern in the gas and oil industries. The effect of sulfur deposition on nickel-based alloy 825 under severe conditions is not well understood. This work investigates the impact of elemental sulfur deposition on Alloy 825 under two conditions using four-point bend test in accordance with NACE TM0316.The results show that alloy 825 samples were not affected by way of SSC, SCC, pitting or other corrosion damage mechanisms in temperature of 90° C, pressure of 75 bar, Chloride level of 1000 ppm, a partial pressure of H2S of 12 bara, and a partial pressure of CO2 of 55 bara with present of elemental sulfur. A further autoclave exposure test was performed in which alloy 825 samples were exposed in 20 bara H2S partial pressure and 57 bara CO2 partial pressure in 21,853 ppm chloride and =150gL-1 elemental sulfur at 190°C for 720 hours. Under this condition, alloy 825 shows environmentally assisted corrosion as well as SCC on all samples. As a conclusion, alloy 825 is not a robust material against elemental sulfur related degradation at high temperature and pressure with high H2S and CO2 environment. Hence, safety risk from elemental sulfur deposition at high temperature should be carefully considered and evaluated when using alloy 825. The limit tested in this paper could provide a reference for selecting alloy 825 in presence of sulfur.
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Product Number:
51323-19041-SG
Author:
Leslie A. Ward, Len J. Krissa, Garry Matocha, Thomas Pickthall
Publication Date:
2023
$20.00
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Product Number:
51323-19044-SG
Author:
Charles Thomas, Liam Rowlands, Keith Lichti, Nathan Gibson
Publication Date:
2023
$20.00
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Product Number:
51324-21201-SG
Author:
Ayman A. Alabdullatif; Lay Seong Teh; Hatam Mehraz; Anaam H. Shaikh Ali
Publication Date:
2024
$40.00
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Product Number:
51321-16755-SG
Author:
Abbey Wing; Winston Robbins, PhD; Gerrit Buchheim, P.E.; Frank Sapienza
Publication Date:
2021
$20.00
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Product Number:
51323-19107-SG
Author:
Ishan Patel, Gheorghe Bota, David Young
Publication Date:
2023
$20.00
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Product Number:
51324-20668-SG
Author:
Gheorghe Bota; Ishan Patel; Peng Jin; David Young
Publication Date:
2024
$40.00
Cheap heavy crudes become attractive for oil refineries to increase their benefit margins but the corrosivity of heavy crudes compels the refinery engineers to blend them with the more expensive light sweet crudes. Crude oil blends with complex composition including organo-sulfur compounds, fatty acids, nitrogen and chlorine compounds become corrosive when processed at high temperatures due to these reactive species. Therefore, maintaining corrosion control is a constant effort in oil refineries, and it involves the use of dedicated corrosion models combined with specific experimental lab procedures and methods. This work is presenting the practical application of a lab testing procedure used for predicting the high temperature corrosivity of different crude fractions that were run successively for different time periods in a specific “flow-through” apparatus. The testing procedure consists of two distinct phases performed in the same apparatus, at the same temperature, and for different time durations. During the first phase of the test, scales are formed using a distilling fraction on metal samples and further, in the second test phase, these preformed scales on samples are exposed without interruption to a different distilling fraction. Thus, the two successive test phases, each using a different distilling fraction, are associated with the “changing feeds” in the distilling tower. Corrosive effects are evaluated by sample weight loss measured in successive fraction tests and in separate tests performed with each of the selected fractions. Experimental results are compared to predictions of a corrosion model for sulfidation and naphthenic acid corrosion.
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Product Number:
51323-19105-SG
Author:
Winston Robbins, Sridhar Srinivasan, Gerrit Buchheim
Publication Date:
2023
$20.00
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