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line pipe
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Image
Published: 01 August 2005
Fig. 5.64 Crack growth in X-65 line pipe steel exposed to air and 3.5% salt water with a superimposed cathodic potential. Source: Ref 5.79
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Image
Published: 01 July 2000
Fig. 7.82 Effects of strain rate upon stress corrosion susceptibility of line pipe steel in 79 °C, 2 N CO 3 /HCO 3 solutions at several potentials relative to SHE. Redrawn from Ref 119
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Image
Published: 01 December 2015
Fig. 7 Intergranular high-pH stress-corrosion crack in line pipe steel. Nital etchant. Original magnification: 400×
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Image
Published: 01 September 2011
Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2008
DOI: 10.31399/asm.tb.ssde.t52310247
EISBN: 978-1-62708-286-0
... Abstract This chapter discusses various factors pertinent to the prevention of corrosion in alloys for petroleum applications and reviews the selection of stainless steels for petroleum applications, including oil country tubular goods, line pipe, offshore platforms, liquefied natural gas...
Abstract
This chapter discusses various factors pertinent to the prevention of corrosion in alloys for petroleum applications and reviews the selection of stainless steels for petroleum applications, including oil country tubular goods, line pipe, offshore platforms, liquefied natural gas vessels, and refinery equipment.
Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2015
DOI: 10.31399/asm.tb.cpi2.t55030338
EISBN: 978-1-62708-282-2
... on American Petroleum Institute API 5L specifications ( Ref 10 ). Typically, maximum composition limits are specified for carbon, manganese, phosphorous, and sulfur. In some cases, other alloying elements are added to improve mechanical properties. Composition and tensile requirements for common line pipe...
Abstract
This chapter discusses the most common causes and contributing factors for external corrosion and stress-corrosion cracking on oil and natural gas pipelines, as well as describes procedures for prevention, mitigation, detection, assessment, and repair. The forms of external corrosion covered include differential cell corrosion, microbiologically influenced corrosion, and stray current corrosion.
Image
Published: 01 July 2000
Fig. 7.123 Corrosion-fatigue-crack-growth rate as a function of stress-intensity range for X-65 line pipe steel in air and at the free corrosion potential in 3.5% NaCl at indicated frequencies and R = 0.2. Corrosion potential = –440 ± 30 mV (SHE). (Note: Original reference includes data
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Image
Published: 01 July 2000
Fig. 7.122 Corrosion-fatigue-crack-growth rate as a function of stress-intensity range for X-65 line pipe steel in air and in 3.5% NaCl solution under cathodic coupling to zinc. Cycled at indicated frequencies and R = 0.2. Coupled potential = –800 ± 10 mV (SHE). (Note: Original reference
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Image
Published: 01 July 2000
Fig. 7.119 Fatigue-crack-growth rates as a function of stress-intensity amplitude for X-65 line pipe steel in air. Frequency 0.1–15 Hz, at R = 0.2. Redrawn from Ref 169
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Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2015
DOI: 10.31399/asm.tb.cpi2.t55030023
EISBN: 978-1-62708-282-2
... in higher resistivity soil. Accelerated corrosion occurs on the foreign line at the point of current discharge. The location of the discharge can be detected because the pipe-to-soil potential is very low at that point. Likewise in an oil or gas field, where the flow-line system or the well casings from...
Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 January 2000
DOI: 10.31399/asm.tb.cub.t66910331
EISBN: 978-1-62708-250-1
... pipe 2.47 2.74 1.74 2.38 PTFE-lined steel 2.62 2.78 2.14 2.70 Ni-Cu Alloy 400, Sch. 5 2.63 2.95 2.28 2.47 Nickel 200, Sch. 5 2.69 3.71 2.32 2.65 Alloy 20, Sch. 40 2.87 4.68 2.41 5.55 Ni-Cu Alloy 400, Sch. 40 3.17 4.95 3.17 4.33 Ni-Cr Alloy 600, Sch. 5 3.23...
Abstract
The challenge of materials selection is to achieve adequate performance at the lowest possible cost. Corrosion resistance is not the only property to be considered in making materials selections. Typical requirements and some of the procedures involved in making a selection and some of the factors that must be considered when determining the corrosion performance of a given material are listed in this chapter. The various steps that might be included in a materials selection process are then examined. These include a review of operating conditions and design, the selection of candidate materials, the in-depth evaluation of each candidate material, fabrication requirements, follow-up monitoring, and final materials selection. Material considerations such as cost, materials properties, and processing and fabrication requirements are subsequently covered. Finally, the chapter provides information on materials selection under general corrosion conditions and under conditions of localized corrosion forms such as pitting, crevice corrosion, and stress-corrosion cracking.
Series: ASM Technical Books
Publisher: ASM International
Published: 01 September 2008
DOI: 10.31399/asm.tb.fahtsc.t51130503
EISBN: 978-1-62708-284-6
... would always be the location of maximum susceptibility to cracking. Using the advantages of modern low-carbon steels and consumables, Nippon Steel (Ref 4) designed a series of commercial low-carbon steels for line pipes that could be welded while maintaining high strength and toughness with equally...
Abstract
Failure analysis of steel welds may be divided into three categories. They include failures due to design deficiencies, weld-related defects usually found during inspection, and failures in field service. This chapter emphasizes the failures due to various discontinuities in the steel weldment. These include poor workmanship, a variety of hydrogen-assisted cracking failures, stress-corrosion cracking, fatigue, and solidification cracking in steel welds. Hydrogen-assisted cracking can appear in four common forms, namely underbead or delayed cracking, weld metal fisheyes, ferrite vein cracking, and hydrogen-assisted reduced ductility.
Image
Published: 01 June 1988
Fig. 10.11 Schematic illustration of equipment used for in-line induction through hardening and tempering of pipe-mill products. Pipe enters from the right, is austenitized, quenched, drained, and tempered. Following tempering, the pipe is transferred to cooling beds for air cooling. From R. M
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Image
in Process Design for Specific Applications
> Elements of Induction Heating: Design, Control, and Applications
Published: 01 June 1988
Fig. 6.18 Plot used to determine power requirements for induction welding of steel pipe. The required power in kilowatts is equal to the product of the line speed (in fpm), the pipe wall thickness (in in.), the width of the heated zone (in in.), and V as determined from the plot. From G. F
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Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2015
DOI: 10.31399/asm.tb.cpi2.t55030089
EISBN: 978-1-62708-282-2
...) for stress relief was beneficial in reducing HAZ attack ( Ref 2 ), despite the previous comments. HAZ/Fusion Line Corrosion of Welded Line Pipe There is a particular case of preferential weldment corrosion worth highlighting in respect to electric-resistance-welded/high-frequency-induction-welded (ERW...
Abstract
This chapter describes issues related to corrosion of carbon steel weldments and remedial measures that have proven successful in specific cases. The forms of corrosion covered includes preferential heat affected zone corrosion, preferential weld metal corrosion, and galvanic corrosion. Industrial case studies demonstrating the necessity for testing each galvanic couple in the environment for which it is intended are presented. The chapter also discusses various factors associated with stress-corrosion cracking in oil refineries.
Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2015
DOI: 10.31399/asm.tb.cpi2.t55030247
EISBN: 978-1-62708-282-2
... up from $589 million for surface piping and facility costs, $463 million in downhole tubing expenses, and $320 million in capital expenditures related to corrosion. The control of corrosion through the use of coatings, metallurgy, nonmetallic materials of construction, cathodic protection, inhibitors...
Abstract
This chapter discusses the particular corrosion problems encountered and the methods of control used in petroleum production and the storage and transportation of oil and gas up to the refinery. It begins by describing those aspects of corrosion that tend to be unique to corrosion as encountered in applications involving oil and gas exploration and production. This is followed by a section reviewing the methods of corrosion control, namely the proper selection of materials, protective coatings, cathodic protection systems, use of inhibitors, use of nonmetallic materials, and control of the environment. The chapter ends with a discussion on the problems encountered and protective measures that are based on the state-of-the-art as practiced daily by corrosion and petroleum engineers and production personnel.
Book: Corrosion of Weldments
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2006
DOI: 10.31399/asm.tb.cw.t51820177
EISBN: 978-1-62708-339-3
... involving the core spray, reactor water cleanup, residual heat removal, control-rod return lines, and isolation condenser lines have also been affected. A schematic of a recirculation piping system representative of one BWR model is shown in Fig. 6 . Piping systems in a typical BWR may have 150 to 200...
Abstract
This chapter reviews weld corrosion in three key application areas: petroleum refining and petrochemical operations, boiling water reactor piping systems, and components used in pulp and paper plants. The discussion of each area addresses general design and service characteristics, types of weld corrosion issues, and prevention or mitigation strategies.
Book: Corrosion of Weldments
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2006
DOI: 10.31399/asm.tb.cw.t51820013
EISBN: 978-1-62708-339-3
... of Welded Line Pipe There is a particular case of preferential weldment corrosion worth highlighting in respect to electric-resistance-welded/high-frequency-induction-welded (ERW/HFI) pipe, where attack of the seam weld HAZ/fusion line can occur in aqueous environments or when exposed to the water...
Abstract
Carbon and low-alloy steels are the most frequently welded metallic materials, and much of the welding metallurgy research has focused on this class of materials. Key metallurgical factors of interest include an understanding of the solidification of welds, microstructure of the weld and heat-affected zone (HAZ), solid-state phase transformations during welding, control of toughness in the HAZ, the effects of preheating and postweld heat treatment, and weld discontinuities. This chapter provides information on the classification of steels and the welding characteristics of each class. It describes the issues related to corrosion of carbon steel weldments and remedial measures that have proven successful in specific cases. The major forms of environmentally assisted cracking affecting weldment corrosion are covered. The chapter concludes with a discussion of the effects of welding practice on weldment corrosion.
Series: ASM Technical Books
Publisher: ASM International
Published: 01 December 2015
DOI: 10.31399/asm.tb.cpi2.t55030292
EISBN: 978-1-62708-282-2
... by the combination of moisture, sulfur components, and oxygen when process equipment is opened to air. Typical applications include linings and tray components in fractionation towers; piping; heat-exchanger tubes; reactor cladding; tubes and tube hangers in furnaces; various components for compressors, turbines...
Abstract
This chapter presents the primary considerations and mechanisms for corrosion and how they are involved in the selection of materials for process equipment in petroleum refineries and petrochemical plants. In addition, specific information on mechanical properties, corrosion, sulfide stress cracking, hydrogen-induced cracking, stress-oriented hydrogen-induced cracking, hydrogen embrittlement cracking, stress-corrosion cracking, velocity-accelerated corrosion, erosion-corrosion, and corrosion control is provided.
Book Chapter
Series: ASM Technical Books
Publisher: ASM International
Published: 01 August 2015
DOI: 10.31399/asm.tb.piht2.t55050335
EISBN: 978-1-62708-311-9
... with epoxy-coated linings on the interior surfaces, the epoxy breaks down between the fifth and tenth years of use. The epoxy comes loose and will collect in strainers or in the quench spray holes of the coils or quench rings ( Ref 3 ). To prevent galvanic corrosion, the piping should not be made...