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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.
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
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.
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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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Series: ASM Handbook
Volume: 9
Publisher: ASM International
Published: 01 December 2004
DOI: 10.31399/asm.hb.v09.a0003737
EISBN: 978-1-62708-177-1
Abstract
This article discusses the specimen preparation of three types of cast and wrought heat-resistant alloys: iron-base, nickel-base, and cobalt-base. Specimen preparation involves sectioning, mounting, grinding, polishing, and etching. The article illustrates the microstructural constituents of cast and wrought heat-resistant alloys. It describes the identification of ferrite by magnetic etching. The transmission electron microscopy examination of the fine strengthening phases in wrought alloys and bulk extraction in heat-resistant alloys are included. The article also reviews the gamma prime phase, gamma double prime phase, eta phase, laves phase, sigma phase, mu phase, and chi phase in wrought heat-resistant alloys.
Series: ASM Handbook
Volume: 9
Publisher: ASM International
Published: 01 December 2004
DOI: 10.31399/asm.hb.v09.a0003767
EISBN: 978-1-62708-177-1
Abstract
This article describes metallographic preparation and examination techniques for stainless steels and maraging steels. It presents a series of micrographs demonstrating microstructural features of these alloys. Procedures used to prepare stainless steels for macroscopic and microscopic examination are similar to those used for carbon, alloy, and tool steels. Cutting and grinding must be carefully executed to minimize deformation because the austenitic grades work harden readily. The high-hardness martensitic grades that contain substantial undissolved chromium carbide are difficult to polish while fully retaining the carbides. Unlike carbon, alloy, and tool steels, etching techniques are more difficult due to the high corrosion resistance of stainless steels and the various second phases that may be encountered. The microstructures of stainless steels can be quite complex. Matrix structures vary according to the type of steel, such as ferritic, austenitic, martensitic, precipitation hardenable, or duplex.
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Published: 01 August 2013
Fig. 4 Erosion- and corrosion-attacked tubes of a biomass-fired boiler pipe panel. Sample courtesy of Häuser & Co. GmbH, Duisburg, Germany.
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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. 15 Creep-rupture strengths of various boiler tube steels at 600 °C (1110 °F). Source: Ref 21
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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. 16 100,000-h creep-rupture strength of various steels used in boiler tubes. TB12 steel has as much as five times the 100,000-h creep-rupture strength of conventional ferritic steels at 600 °C (1110 °F). This allows an increase in boiler tube operating temperature of 120 to 130 °C (215
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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. 9 Estimated design allowable stresses (Section VIII of ASME Boiler and Pressure Vessel Code) as a function of temperature for modified 9Cr-1Mo steel, standard 9Cr-1Mo, 2 1 4 Cr-1Mo steel, and 304 stainless steel. Source: Ref 7
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Published: 01 January 2005
Fig. 37 Short-term and rapid overheating of a steel boiler tube (reheater, superheater, or similar—source unknown) resulted in a longitudinal “fish-mouth” rupture. The tube had experienced elevated temperatures (455 to >730 °C, or 850 to >1350 °F) where the metal strength is markedly
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in Corrosion in Supercritical Water—Ultrasupercritical Environments for Power Production
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 1 Simplified water path in a large supercritical utility boiler, with a single reheat step
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in Corrosion in Supercritical Water—Ultrasupercritical Environments for Power Production
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 2 Schematic of a supercritical sliding pressure Benson boiler, Tachibana-Wan No. 2, 25.0 MPa/600 °C/610 °C/610 °C. Source: Ref 5
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in Corrosion in Supercritical Water—Ultrasupercritical Environments for Power Production
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 3 Rankine cycle for a subcritical boiler. Source: Ref 3
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in Corrosion in Supercritical Water—Ultrasupercritical Environments for Power Production
> Corrosion: Environments and Industries
Published: 01 January 2006
Fig. 4 Rankine cycle for a supercritical boiler. Source: Ref 3
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