The effect of mono ethylene glycol on the top of line corrosion rate of low carbon steel in acetic acid and elevated temperature environment

Abstract Corrosion rate data are presented for low carbon steel in (1) a combination of sulfur dioxide, water vapor and air, and (2) aqueous solutions of sulfurous acid in the absence of air, at ordinary temperature. Information as to the nature of the corrosion products is presented and it is shown that this depends on the place in which the corrosion takes place to an important extent.

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Corrosion behaviors of iron, chromium, nickel, low-carbon steel and four types of stainless steels in liquid antimony-tin alloy

CORROSION ◽

10.5006/3820 ◽

2021 ◽

Author(s):

Wei Liu ◽

Huayi Yin ◽

Kaifa Du ◽

Bing Yang ◽

Dihua Wang

Keyword(s):

Carbon Steel ◽

Corrosion Rate ◽

Stainless Steels ◽

Liquid Metals ◽

Low Carbon Steel ◽

Solid Substrate ◽

Low Carbon ◽

Corrosion Resistant ◽

Corrosion Behaviors ◽

Iron Chromium

Corrosion-resistant metals and alloys towards liquid metals determine the service performances and lifetime of the devices employing liquid metals. This paper studies the static corrosion behaviors of iron, chromium, nickel, low carbon steel, and four types of stainless steels (SS410, SS430, SS304, SS316L) in liquid Sb-Sn at 500 oC, aiming to screen corrosion-resistant SS for Li||Sb-Sn liquid metal batteries (LMBs). The corrosion rates of Fe and Ni are 0.94 μm h-1 and 6.03 μm h-1 after 160 h’s measurement, respectively. Cr shows a low corrosion rate of < 0.05μm h-1, which is due to the formation of a relatively stable Cr-Sb layer that may be able to prevent the interdiffusion between the solid substrate and liquid Sb-Sn. Ni has a high corrosion rate because the formed Ni-Sb and Ni-Sn compounds are soluble in the liquid Sb-Sn. The corrosion products of both pure metals and SS can be predicted by thermodynamic and phase diagram analysis. Among the four types of SS, SS430 shows the best corrosion resistance towards liquid Sb-Sb with a corrosion rate of 0.19 μm h-1. Therefore, a liquid Sb-Sn resistant material should have a high Cr content and a low Ni content, and this principle is applicable to design metallic materials not only for LMBs but also for other devices employing liquid Sb- and Sn-containing liquid metals.

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Microstructure and Wear Properties of Electrodeposited Ni-B-Al2O3 Composite Coating on Low Carbon Steel at Elevated Temperature

Journal of Materials Engineering and Performance ◽

10.1007/s11665-021-06290-2 ◽

2021 ◽

Author(s):

Serdar Aslan ◽

Erhan Duru

Keyword(s):

Elevated Temperature ◽

Carbon Steel ◽

Composite Coating ◽

Low Carbon Steel ◽

Low Carbon ◽

Wear Properties ◽

Al2o3 Composite

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The Corrosion of Carbon Steel and Stainless Steel in Simulated Geothermal Media

Australian Journal of Chemistry ◽

10.1071/ch9851133 ◽

1985 ◽

Vol 38 (8) ◽

pp. 1133 ◽

Cited By ~ 14

Author(s):

BG Pound ◽

MH Abdurrahman ◽

MP Glucina ◽

GA Wright ◽

RM Sharp

Keyword(s):

Carbon Steel ◽

Corrosion Rate ◽

Stainless Steels ◽

Polarization Resistance ◽

Iron Sulfide ◽

Low Carbon Steel ◽

Passive Films ◽

Low Carbon ◽

Corrosion Rates ◽

Good Agreement

The corrosion rates of low-carbon steel, and 304, 316 and 410/420 stainless steels in simulated geothermal media containing hydrogen sulfide have been measured by means of the polarization resistance technique. Good agreement was found between weight-loss and polarization resistance measurements of the corrosion rate for all the metals tested. Carbon steel formed a non-adherent film of mackinawite (Fe1 + xS). The lack of protection afforded to the steel by the film resulted in an approximately constant corrosion rate. The stainless steels also exhibited corrosion rates that were independent of time. However, the 410 and 420 alloys formed an adherent film consisting mainly of troilite ( FeS ) which provided only limited passivity. In contrast, the 304 and 316 alloys appeared to be essentially protected by a passive film which did not seem to involve an iron sulfide phase. However, all the stainless steels, particularly the 410 and 420 alloys, showed pitting, which indicated that some breakdown of the passive films occurred.

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The inhibition performance of mono-ethylene glycol on corrosion rate of x-80 grade carbon steel in saturated brine environment.

African Journal of Engineering and Environment Research ◽

10.37703/ajoeer.org.ng/q12020/03 ◽

2020 ◽

Vol 1 (1) ◽

Keyword(s):

Acetic Acid ◽

Charge Transfer ◽

Carbon Steel ◽

Corrosion Rate ◽

Ethylene Glycol ◽

Oil And Gas ◽

Gas Production ◽

Electrochemical Measurements ◽

Co2 Corrosion ◽

Formation Water

The formation/deposition of hydrate and scale in gas production and transportation pipeline has continue to be a major challenge in the oil and gas industry. Pipeline transport is one of the most efficient, reliable and safer means of transporting petroleum products from the well sites to either the refineries or to the final destinations. Acetic acid (HAc), is formed in the formation water which also present in oil and gas production and transportation processes. Acetic acid aids corrosion in pipelines and in turn aids the formation and deposition of scales which may eventually choke off flow. Most times, Monethylene Glycol (MEG) is added into the pipeline as an antifreeze and anticorrosion agent. Some laboratory experiments have shown that the MEG needs to be separated from unwanted substance such as HAc that are present in the formation water to avoid critical conditions in the pipeline. Internal pipeline corrosion slows and decreases the production of oil and gas when associated with free water and reacts with CO2 and organic acid by lowering the integrity of the pipe. In this study, the effect of Mono-Ethylene Glycol (MEG) and Acetic acid (HAc) on the corrosion rate of X-80 grade carbon steel in CO2 saturated brine were evaluated at 25oC and 80oC using 3.5% NaCl solution in a semi-circulation flow loop set up. Weight loss and electrochemical measurements using the linear polarization resistance (LPR) and electrochemical impedance spectroscope (EIS) were used in measuring the corrosion rate as a function of HAc and MEG concentrations. The results obtained so far shows an average corrosion rate increases from 0.5 to 1.8 mm/yr at 25oC, and from 1.2 to 3.5 mm/yr at 80oC in the presence of HAc. However, there are decrease in corrosion rate from 1.8 to 0.95 mm/yr and from 3.5 to 1.6mm/yr respectively at 25oC and 80oC on addition of 20% and 80% MEG concentrations to the solution. It is also noted that the charge transfer with the electrochemical measurements (EIS) results is the main corrosion controlling mechanism under the test conditions. The higher temperature led to faster film dissolution and higher corrosion rate in the presence of HAc. The EIS results also indicate that the charge transfer controlled behaviour was as a result of iron carbonate layer accelerated by the addition of different concentrations of MEG to the system. Key words: CO2 corrosion, Carbon steel, MEG, HAc, Inhibition, Environment.

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Influence of Pause in Stress Alternation on the Fatigue of a Low Carbon Steel at Elevated Temperature

Transactions of the Japan Society of Mechanical Engineers ◽

10.1299/kikai1938.25.1070 ◽

1959 ◽

Vol 25 (159) ◽

pp. 1070-1074 ◽

Cited By ~ 1

Author(s):

Shuji TAIRA ◽

Yasunori MURAKAMI ◽

Ryoichi KOTERAZAWA

Keyword(s):

Elevated Temperature ◽

Carbon Steel ◽

Low Carbon Steel ◽

Low Carbon

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PENGARUH BASIC SEDIMENT AND WATER TERHADAP LAJU KOROSI PIPA X52 DAN A53 PADA MEDIA OIL SLUDGE.

ROTOR ◽

10.19184/rotor.v10i1.5141 ◽

2017 ◽

Vol 10 (1) ◽

pp. 13

Author(s):

Naufan Arviansyah ◽

Sumarji Sumarji ◽

Digdo Listyadi Setyawan

Keyword(s):

Weight Loss ◽

Carbon Steel ◽

Corrosion Rate ◽

Low Carbon Steel ◽

Measuring Method ◽

Oil Sludge ◽

Uniform Corrosion ◽

Low Carbon ◽

Weight Loss Method ◽

Loss Method

This research have a purpuse to know corrosion rate in pipe X52 and A53 at oil sludge media caused BS and W. Corrosion is a damage of metal that occurs because reaction between metal with environtment and produce unwanted of corrosion product. Pipe X52 and A53 is a type of low carbon steel that use for fluid transportation system in industry. Oil sludge is a sediment of crude oil from main gathering storage and containing variouses elements. Oil sludge have a one of element is Basic Sediment and Water that is can make corrosion happen to distribution pipes. Measuring Method used in this research is weight loss method. The result of corrosion rate in Oil Sludge media containing 30,17% BS and W for pipe A53 is 1,64 x 10-2 mmpy and the result for pipa X52 is 2,47 x 10-2 mmpy. The result of corrosion rate in Oil Sludge media containing 60,67% BS and W for pipe A53 is 2,12 x 10-2 mmpy and for pipe X52 the result is 3,13 x 10-2 mmpy. The result of this research showed pipe A53 have more resistance than pipe X52. The corrosion is classified as uniform corrosion. Keywords : A53, Weight Loss, Oil Sludge, X52.

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