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hydrogen sulfide
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in Elevated-Temperature Properties of Ferritic Steels
> Properties and Selection: Irons, Steels, and High-Performance Alloys
Published: 01 January 1990
Fig. 31 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of (a) carbon steel, (b) 5Cr-0.5Mo steel, and (c) 9Cr-1Mo steel. These corrosion rates are based on the use of gas oil desulfurizers; corrosion rates with naphtha desulfurizers may be slightly
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 7 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of carbon steel (naphtha desulfurizers). 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 8 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of carbon steel (gas oil desulfurizers). 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 9 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of 5Cr-0.5Mo steel (naphtha desulfurizers). 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 10 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of 5Cr-0.5Mo steel (gas oil desulfurizers). 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 11 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of 9Cr-1Mo steel (naphtha desulfurizers). 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 12 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of 9Cr-1Mo steel (gas oil desulfurizers). 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 13 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of 12% Cr stainless steel. 1 mil/yr=0.025 mm/yr. Source: Ref 112
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in Corrosion in Petroleum Refining and Petrochemical Operations
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 14 Effect of temperature and hydrogen sulfide content on high-temperature H 2 S/H 2 corrosion of 18Cr-8Ni austenitic stainless steel. 1 mil/yr=0.025 mm/yr. Source: Ref 112
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Published: 01 January 1996
Fig. 69 Fatigue crack growth rates in crude oil with two levels of hydrogen sulfide content at three frequencies
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Series: ASM Handbook
Volume: 13C
Publisher: ASM International
Published: 01 January 2006
DOI: 10.31399/asm.hb.v13c.a0004104
EISBN: 978-1-62708-184-9
... Abstract This article provides information on predesign surveys and the various testing procedures associated with wastewater treatment plants. These include soil testing, atmospheric testing, and hydrogen sulfide testing. The primary parameters that influence the production of sulfides within...
Abstract
This article provides information on predesign surveys and the various testing procedures associated with wastewater treatment plants. These include soil testing, atmospheric testing, and hydrogen sulfide testing. The primary parameters that influence the production of sulfides within the piping system that transports the wastewater to the treatment facility are discussed. The article describes the corrosion performance of various materials in the soil, fluid, and atmospheric exposures. These include concrete, steel, ductile iron, aluminum, copper, brass, stainless steel, and coatings used for wastewater facilities.
Book: Fatigue and Fracture
Series: ASM Handbook
Volume: 19
Publisher: ASM International
Published: 01 January 1996
DOI: 10.31399/asm.hb.v19.a0002395
EISBN: 978-1-62708-193-1
... of corrosion fatigue crack initiation and prevention of corrosion fatigue. It presents case histories of fatigue failure of various steel components. The article reviews the failure of coiled tubing in a drilling application and the failure of coiled tubing due to hydrogen sulfide exposure, with examples...
Abstract
This article provides information on fracture toughness and fatigue crack growth of structural steels. It describes fatigue life behavior in terms of unnotched fatigue limits, notch effects, axial strain-life fatigue, and mean stress effects. The article analyzes the mechanisms of corrosion fatigue crack initiation and prevention of corrosion fatigue. It presents case histories of fatigue failure of various steel components. The article reviews the failure of coiled tubing in a drilling application and the failure of coiled tubing due to hydrogen sulfide exposure, with examples.
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Published: 01 June 2024
Fig. 31 Hydrogen blistering failure from a heat exchanger that was operating in a hydrogen sulfide environment. ASTM A516 grade 70 plain carbon steel plate. The inner surface is toward the bottom of the image in (b). (a) Macroscopic appearance of the failure. (b) Profile of the blister near
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Series: ASM Handbook
Volume: 13A
Publisher: ASM International
Published: 01 January 2003
DOI: 10.31399/asm.hb.v13a.a0003700
EISBN: 978-1-62708-182-5
... ions and resulting in a low pH environment. Other contaminants, carbon dioxide, oxides of sulfur and nitrogen, hydrogen sulfide, oxygen, and low-molecular- weight organic acids will also dissolve into the condensed water. The concentration and resulting corrosive effect of these materials is generally...
Abstract
This article provides useful information on the occurrence of corrosion in crude oil refinery units, namely, crude unit, catalytic and thermal cracking units, hydroprocessing units, amine sweetening units, and sour water units. Types and applications of corrosion inhibitors, namely, neutralizers, filming inhibitors, scavengers, microbiocides, and anti-foulants and scale inhibitors, are reviewed. The article describes the direct and indirect corrosion monitoring methods used to reduce equipment damage due to corrosion events and to assess the reliability and useful service life of process equipment.
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Published: 01 January 2003
Fig. 4 Protective and nonprotective scales formed on alloy 800. (a) Cr 2 O 3 -base protective oxide scale formed in sulfur-free oxidizing gas. (b) Sulfide-oxide scale formed in reducing conditions containing hydrogen sulfide. Courtesy of I.G. Wright, Battelle Columbus Division
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in Elevated-Temperature Properties of Stainless Steels
> Properties and Selection: Irons, Steels, and High-Performance Alloys
Published: 01 January 1990
Fig. 11 Elevated-temperature corrosion rates of steels in hydrogen and hydrogen sulfide environments (H 2 S concentrations above 1 mole %). Source: Ref 20
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Published: 01 January 2002
Fig. 8 Stepwise cracking of a low-strength pipeline steel exposed to hydrogen sulfide (H 2 S). 6×
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Published: 01 January 2006
Fig. 2 Corrosion of low-alloy steels in syngas environments. Plant data are compared to laboratory data for various hydrogen sulfide atmospheres.
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Published: 15 January 2021
Fig. 8 Stepwise cracking of a low-strength pipeline steel exposed to hydrogen sulfide (H 2 S). Original magnification: 6×
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Published: 01 January 1990
Fig. 65 Relationship between specimen hardness and time to failure in aqueous 0.5% acetic acid saturated with hydrogen sulfide for martensitic and precipitation-hardenable stainless steels. Source: Ref 370
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