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Series: ASM Handbook
Volume: 11A
Publisher: ASM International
Published: 30 August 2021
DOI: 10.31399/asm.hb.v11A.a0006825
EISBN: 978-1-62708-329-4
... Abstract Failures in boilers and other equipment taking place in power plants that use steam as the working fluid are discussed in this article. The discussion is mainly concerned with failures in Rankine cycle systems that use fossil fuels as the primary heat source. The general procedure...
Abstract
Failures in boilers and other equipment taking place in power plants that use steam as the working fluid are discussed in this article. The discussion is mainly concerned with failures in Rankine cycle systems that use fossil fuels as the primary heat source. The general procedure and techniques followed in failure investigation of boilers and related equipment are discussed. The article is framed with an objective to provide systematic information on various damage mechanisms leading to the failure of boiler tubes, headers, and drums, supplemented by representative case studies for a greater understanding of the respective damage mechanism.
Series: ASM Handbook
Volume: 13C
Publisher: ASM International
Published: 01 January 2006
DOI: 10.31399/asm.hb.v13c.a0004154
EISBN: 978-1-62708-184-9
... Abstract This article briefly describes water and steam chemistry, which influence the effect of corrosion in boilers. The appropriate control measures to prevent corrosion in boilers are also presented. The article provides a discussion on the common causes of fluid-side corrosion such as flow...
Abstract
This article briefly describes water and steam chemistry, which influence the effect of corrosion in boilers. The appropriate control measures to prevent corrosion in boilers are also presented. The article provides a discussion on the common causes of fluid-side corrosion such as flow-accelerated corrosion, oxygen pitting, chelant corrosion, caustic corrosion, acid corrosion, organic corrosion, phosphate corrosion, hydrogen damage, and corrosion-assisted cracking.
Series: ASM Handbook
Volume: 13C
Publisher: ASM International
Published: 01 January 2006
DOI: 10.31399/asm.hb.v13c.a0004156
EISBN: 978-1-62708-184-9
... Abstract The presence of certain impurities in coal and oil is responsible for the majority of fireside corrosion experienced in utility boilers. In coal, the primary impurities are sulfur, alkali metals, and chlorine. The most detrimental impurities in fuel oil are vanadium, sodium, sulfur...
Abstract
The presence of certain impurities in coal and oil is responsible for the majority of fireside corrosion experienced in utility boilers. In coal, the primary impurities are sulfur, alkali metals, and chlorine. The most detrimental impurities in fuel oil are vanadium, sodium, sulfur, and chlorine. This article describes the two categories of fireside corrosion based on location in the furnace: waterwall corrosion in the lower furnace and fuel ash corrosion of superheaters and reheaters in the upper furnace. It discusses prevention methods, including changes to operating parameters and application of protective cladding or coatings.
Series: ASM Handbook
Volume: 13C
Publisher: ASM International
Published: 01 January 2006
DOI: 10.31399/asm.hb.v13c.a0004157
EISBN: 978-1-62708-184-9
... Abstract This article describes the corrosion modes in a waste-to-energy boiler. It discusses the corrosion protection and alloy performance with an emphasis on two main areas of the boiler: furnace water walls and super heaters. waste-to-energy boiler corrosion protection high...
Series: ASM Handbook Archive
Volume: 11
Publisher: ASM International
Published: 01 January 2002
DOI: 10.31399/asm.hb.v11.a0001816
EISBN: 978-1-62708-180-1
... Abstract This article explains the main types and characteristic causes of failures in boilers and other equipment in stationary and marine power plants that use steam as the working fluid with examples. It focuses on the distinctive features of each type that enable the failure analyst...
Abstract
This article explains the main types and characteristic causes of failures in boilers and other equipment in stationary and marine power plants that use steam as the working fluid with examples. It focuses on the distinctive features of each type that enable the failure analyst to determine the cause and suggest corrective action. The causes of failures include tube rupture, corrosion or scaling, fatigue, erosion, and stress-corrosion cracking. The article also describes the procedures for conducting a failure analysis.
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in Corrosion in Supercritical Water—Ultrasupercritical Environments for Power Production
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 5 The evolution of ferritic steels for boilers. Generations are categorized by the 10 5 h creep-rupture strength at 600 °C. Source: Ref 7 , 10
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in Corrosion in Supercritical Water—Ultrasupercritical Environments for Power Production
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 7 The evolution of austenitic steels for boilers. {#} indicates 10 5 h creep-rupture strength at 600 °C, 2 Mpa. Source: Ref 7 , 10
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Published: 01 January 2006
Fig. 6 Maximum coal ash corrosion rates of alloys in ultrasupercritical boilers as a function of chromium concentration. Squares and diamonds are data from different test loops.
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Published: 01 January 2006
Fig. 7 Maximum coal ash corrosion rates of alloys in ultrasupercritical boilers as a function of Cr+Ni concentration. Squares and diamonds are data from different test loops.
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Published: 01 January 1987
Fig. 578 Creep failure of steam boiler superheater tube. Material: normalized and tempered ASME SA213, grade T22 (2.25Cr-1Mo steel). Cracking occurred at a hot spot due to long-time exposure to tensile stresses induced by the internal pressure and service temperatures up to 705 °C (1300 °F
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Published: 01 January 2002
Fig. 16 Failed polyoxymethylene gear wheel that had been in operation in a boiler-room environment. 305×. Source: Ref 53
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Published: 01 January 2002
Fig. 7 Thin-lip rupture in a boiler tube that was caused by rapid overheating. This rupture exhibits a “cobra” appearance as a result of lateral bending under the reaction force imposed by escaping steam. The tube was a 64-mm (2 1 2 -in.) outside-diameter × 6.4-mm (0.250-in.) wall
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Published: 01 January 2002
Fig. 9 Microstructures of specimens from carbon steel boiler tubes subjected to prolonged overheating below Ac 1 . (a) Voids (black) in grain boundaries and spheroidization (light, globular), both of which are characteristic of tertiary creep. 250×. (b) Intergranular separation adjacent
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Published: 01 January 2002
Fig. 10 Typical microstructures of 0.18% C steel boiler tubes that ruptured as a result of rapid overheating. (a) Elongated grains near tensile rupture resulting from rapid overheating below the recrystallization temperature. (b) Mixed structure near rupture resulting from rapid overheating
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Published: 01 January 2002
Fig. 12 Plots of scale thickness versus temperature for two sizes of boiler tubes and two values of heat flux. (a) and (b) The effect of scale thickness on the temperature gradient across the scale. (c) and (d) The effect of scale thickness on the temperature of the metal at the outer surface
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Published: 01 January 2002
Fig. 18 Micrograph of an etched specimen from a carbon steel boiler tube. Decarburization and discontinuous intergranular cracking resulted from hydrogen damage. 250×
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Published: 01 January 2002
Fig. 20 Hydrogen damage (dark area) in a carbon steel boiler tube. The tube cross section was macroetched with hot 50% hydrochloric acid.
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Published: 01 January 2002
Fig. 22 Carbon steel boiler tube that ruptured due to hydrogen damage.
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Published: 01 January 2002
Fig. 31 Stationary boiler in which a carbon steel water-wall tube failed by fatigue fracture at the weld joining the tube to a dust bin. (a) Illustration of a portion of the boiler showing location of failure. Dimensions given in inches. (b) Photograph of fractured tube; fatigue crack
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