The document provides a sample exam with questions for the API 571 certification exam. It includes 14 multiple choice questions covering various corrosion and failure mechanisms that can impact piping and equipment in refineries and petrochemical plants such as CO2 corrosion, hydrogen cracking, amine cracking, and more. The questions assess knowledge of materials selection, corrosion prevention methods, and identification of causes of failures.
This document summarizes API STD 521 Part-I, which provides guidance on overpressure protection for refinery equipment. It discusses overpressure causes and protection philosophies. It also lists the minimum recommended contents for relief system designs and flare header calculations. These include analyzing overpressure causes, operating conditions, relief device sizing, and documentation of simulation inputs and outputs. Various overpressure causes are outlined, such as closed outlets, absorbent or cooling failures, accumulation of non-condensables, abnormal heat input, explosions, and depressurizing. Protection measures against these causes like relief valves, rupture disks, and explosion prevention are also mentioned.
1) A steam explosion at a refinery in Belgium killed two technicians working on a leaking valve. The bonnet separated from the valve body due to failure of 14 out of 20 stud bolts securing it, which were degraded by stress corrosion cracking.
2) An investigation found the valve had a design flaw that put excessive stress on the stud bolts. Several leaks over time exposed the bolts to corrosive conditions, degrading them until one failed during maintenance, causing the explosion.
3) Lessons included the need to thoroughly inspect stud bolts and joints for signs of cracking or corrosion, especially after periods of leakage or being out of service, and considering backup supports when risks are unknown.
This document provides an overview and summary of API 579-1/ASME FFS-1, which provides guidance for conducting Fitness-For-Service (FFS) assessments to demonstrate the structural integrity of in-service components that may contain flaws or damage. It describes the background, scope, assessment levels, acceptance criteria, procedures, and organization of the standard. The standard can be used to qualify components for continued operation or re-rating using different assessment levels from simplified screening to detailed analysis.
This document provides an introduction and overview of the book "Power Piping: The Complete Guide to ASME B31.1" by Charles Becht IV. It discusses the book's coverage of the ASME B31.1 code for power piping systems, the qualifications and experience of the author, and the book's table of contents. The introduction also provides brief biographies of Charles Becht and an overview of his extensive experience with pressure vessels and piping codes and standards.
The document provides an overview of the ASME B31.3 Process Piping Code. It discusses the code's philosophy, organization, history, scope, fluid service categories, and application. Key points include that B31.3 applies to process piping systems in chemical, petroleum, and other plants. It covers piping for various fluids and has specific requirements for Category M and high pressure fluid services. The code is organized into chapters that address design, materials, components, fabrication, inspection, and other topics.
This document provides an overview of key concepts in piping system design including:
1. It describes the basic components of a piping system including pipes, fittings, valves, instruments, supports, and discusses terminal connections and insulation.
2. It outlines the process of developing a piping system layout from defining flow requirements to creating piping and instrumentation diagrams (P&IDs) and 3D models.
3. It highlights important design considerations like accessibility, orientation, straight pipe lengths, drainage and ventilation.
1. The document discusses the importance of interdisciplinary interface engineering for electrical projects and describes various types of interfaces and deliverables that must be coordinated between electrical and other disciplines like process, piping, civil, and instrumentation.
2. It provides examples of typical electrical deliverables that interface with other groups and deliverables received from other groups including plans, diagrams, schedules, specifications and calculations.
3. Maintaining proper documentation through methods like document control indexes, distribution matrices, notes of meetings and memos is important to facilitate interface engineering and coordination between groups.
This document summarizes API STD 521 Part-I, which provides guidance on overpressure protection for refinery equipment. It discusses overpressure causes and protection philosophies. It also lists the minimum recommended contents for relief system designs and flare header calculations. These include analyzing overpressure causes, operating conditions, relief device sizing, and documentation of simulation inputs and outputs. Various overpressure causes are outlined, such as closed outlets, absorbent or cooling failures, accumulation of non-condensables, abnormal heat input, explosions, and depressurizing. Protection measures against these causes like relief valves, rupture disks, and explosion prevention are also mentioned.
1) A steam explosion at a refinery in Belgium killed two technicians working on a leaking valve. The bonnet separated from the valve body due to failure of 14 out of 20 stud bolts securing it, which were degraded by stress corrosion cracking.
2) An investigation found the valve had a design flaw that put excessive stress on the stud bolts. Several leaks over time exposed the bolts to corrosive conditions, degrading them until one failed during maintenance, causing the explosion.
3) Lessons included the need to thoroughly inspect stud bolts and joints for signs of cracking or corrosion, especially after periods of leakage or being out of service, and considering backup supports when risks are unknown.
This document provides an overview and summary of API 579-1/ASME FFS-1, which provides guidance for conducting Fitness-For-Service (FFS) assessments to demonstrate the structural integrity of in-service components that may contain flaws or damage. It describes the background, scope, assessment levels, acceptance criteria, procedures, and organization of the standard. The standard can be used to qualify components for continued operation or re-rating using different assessment levels from simplified screening to detailed analysis.
This document provides an introduction and overview of the book "Power Piping: The Complete Guide to ASME B31.1" by Charles Becht IV. It discusses the book's coverage of the ASME B31.1 code for power piping systems, the qualifications and experience of the author, and the book's table of contents. The introduction also provides brief biographies of Charles Becht and an overview of his extensive experience with pressure vessels and piping codes and standards.
The document provides an overview of the ASME B31.3 Process Piping Code. It discusses the code's philosophy, organization, history, scope, fluid service categories, and application. Key points include that B31.3 applies to process piping systems in chemical, petroleum, and other plants. It covers piping for various fluids and has specific requirements for Category M and high pressure fluid services. The code is organized into chapters that address design, materials, components, fabrication, inspection, and other topics.
This document provides an overview of key concepts in piping system design including:
1. It describes the basic components of a piping system including pipes, fittings, valves, instruments, supports, and discusses terminal connections and insulation.
2. It outlines the process of developing a piping system layout from defining flow requirements to creating piping and instrumentation diagrams (P&IDs) and 3D models.
3. It highlights important design considerations like accessibility, orientation, straight pipe lengths, drainage and ventilation.
1. The document discusses the importance of interdisciplinary interface engineering for electrical projects and describes various types of interfaces and deliverables that must be coordinated between electrical and other disciplines like process, piping, civil, and instrumentation.
2. It provides examples of typical electrical deliverables that interface with other groups and deliverables received from other groups including plans, diagrams, schedules, specifications and calculations.
3. Maintaining proper documentation through methods like document control indexes, distribution matrices, notes of meetings and memos is important to facilitate interface engineering and coordination between groups.
The document summarizes the key changes and new features in Version 4.40 of the CAESAR II pipe stress analysis software. Some of the main updates include revised piping codes, addition of the B31.11 code, expanded static load case options, automatic generation of hydrotest load cases, updates to the 3D graphics, and addition of new configuration options. The installation process for Version 4.40 is described, which includes running an installation driver from the included CD-ROM.
This Presentation is about the basic fundamentals one needs to know to begin Piping Engineering. All the basic formulas and questions that are usually asked in interviews are answered in this presentation. Feel free to ask any doubts in the comments and iI may try my best to answer them for you.
This document outlines welding standards SAES-W-010 through SAES-W-013 from Saudi Aramco. SAES-W-010 covers welding requirements for pressure vessels and discusses approved welding processes, preheat and postweld heat treatment requirements, and requirements for hardness testing and inspections. SAES-W-011 covers on-plot piping and discusses approved welding processes, weld procedures, inspections requirements and preheat/postweld heat treatment. SAES-W-012 covers pipelines and discusses approved welding processes, procedures, preheat requirements and workmanship. Finally, SAES-W-013 covers offshore structures and lists additional requirements beyond API RP-2A and AWS D1.1
Piping Training course-How to be an Expert in Pipe & Fittings for Oil & Gas c...Varun Patel
Course Description
Piping a must know skill to work in Oil & Gas and similar Process Industries.
Oil and Gas industry is become a very competitive in the current time. Getting right mentor and right exposer within industry is difficult. With limited training budget spent by company on employee training, it is difficult to acquire the knowledge to success.
Knowing cross-functional skill give you an edge over others in your career success.
This course design based on years of field experience to ensure student will comprehend technical details easily and enjoy overall journey.
Learn in detail every aspect of Pipe & Pipe Fittings used in process industry
•Different types of Pipe, Pipe fittings (Elbow, Tee, reducers, Caps etc.), Flanges, Gaskets, Branch Connection, Bolting materials
•Materials (Metal-Carbon Steel, Stainless Steel, Alloy Steel etc. Non-Metal- PVC/VCM, HDPE, GRE-GRP etc.)
•Manufacturing methods
•Heat treatment requirements
•Inspection and Testing requirements (Non Destructive Testing, Mechanical & Chemical testing)
•Dimensions & Markings requirements
•Code & Standard used in piping
Content and Overview
With 2 hours of content including 30 lectures & 8 Quizzes, this course cover every aspect of Pipe, Pipe fittings, flanges, gaskets, branch connections and bolting material used in Process Piping.
This Course is divided in three parts.
1st part of the course covers fundamental of process industries. In this Part, you will learn about fundamental process piping. You will also learn about Code, Standard & Specification used in process industries.
2nd part cover various types of material used in process industries. In this part, you will learn about Metallic and Non-Metallic material used to manufacture pipe and other piping components.
3rd parts covers in detail about pipe and piping components used in Process piping. In this part we will learn about Industry terminology of Piping components, types of industrial material grade used in manufacturing and entire manufacturing process of these components. You will learn about different manufacturing methods, Heat treatment requirements, Destructive and Non-destructive testing, Visual & Dimensional inspection and Product marking requirements.
Upon completion, you will be able to use this knowledge direct on your Job and you can easily answer any interview question on pipe & fittings.
Piping Design Course is very Important today. Basically, Piping is the work of Providing and Maintaining the Water Supply, Replacing Pipes and Pipe Work. SEA has trained & certified more than 3000 Engineers & Individuals in last five ( 5 ) years in different engineering disciplines and various sectors which include Oil and Gas , Petrochemicals , Refineries , Power Plant , Aeronautics & Construction projects etc. SEA certification / qualification is accepted and recognized by major National & International companies in the world including India , Saudi Arabia , UAE , Kuwait , Qatar , Bahrain , Oman , Jordan , Iraq , Iran , Yemen , Nigeria , Sudan , Libya , Turkey ,Portugal, Cameroon, Congo & other countries. Our SEA certified Engineers are already working in the above said countries.
Process piping fundamentals, codes and standards module 1BHARAT BELLAD
This document provides an overview of process piping fundamentals, codes, and standards. It covers topics such as pipe sizes, schedules, dimensions, materials, pressure ratings, and applicable design codes. The document is the first module in a nine-part course that introduces piping engineering concepts. It is divided into three chapters that cover piping systems basics, definitions and terminology, and relevant codes and standards like ASME B31.
This presentation describes the considerations involved in selecting the shell and tube exchanger according to TEMA Designations. Also, it helps to identify whether fluid should be sent tube side or shell side
Here's a presentation on piping engineering in PDF format, now available for all. This presentation covers the basics points of piping for our EPC industry. This presentation covers various aspects of piping engineering
Klaus P. Redmann is the Director of Quality at Disc Spring Technology, LLC. He was born in Germany and received his Masters in Chemical Engineering in 1977. His first job after university brought him to the US, where he has resided for 36 years. In addition to his role at DST, Klaus owns Redmann Quality Engineering Services, which performs quality assurance services for nuclear fuel fabrication. Klaus has extensive experience in quality systems auditing and is certified in quality engineering.
The document outlines the key engineering deliverables and responsibilities of different engineering disciplines for a project. It discusses the core deliverables and interdependencies between process, mechanical, piping, control systems, electrical, civil, structural, and architectural disciplines. Feedback from attendees is requested at the end.
This document provides standards for piping design, layout, and stress analysis. It covers topics such as design and layout considerations including numbering systems, safety, clearance, pipe routing, valves, equipment piping, and stress analysis criteria. The standards are intended to replace individual company specifications and be used in existing and future offshore oil and gas developments. It references other NORSOK and international standards and does not cover all instrument control piping, risers, sanitary piping, or GRP piping.
Safety is the most important factor in designing a process system. Some undesired conditions might happen leading to damage in a system. Control systems might be installed to prevent such conditions, but a second safety device is also needed. One kind of safety device which is commonly used in the processing industry is the relief valve. A relief valve is a type of valve to control or limit the pressure in a system by allowing the pressurised fluid to flow out from the system.
This document provides guidelines for selecting, sizing, and specifying relief devices such as pressure relief valves and rupture disks. It discusses general criteria for relief device selection, mechanical design considerations, and specific selection criteria for different services. It also covers relief device calculations, requisitioning, specifications, identification, protection, packaging, and documentation. The guidelines are based on standards from ASME, API, and ISO, and are intended to help achieve maximum technical and economic benefit from standardization when designing oil, gas, chemical, and other processing facilities.
This document provides an overview of ASME Boiler and Pressure Vessel Codes. It discusses the objectives and benefits of codes and standards, and describes the ASME Code system and some of its key sections. It focuses on introducing ASME Section VIII Division 1, covering the scope and exclusions of this section. Key topics covered include design requirements, material specifications, fabrication methods, weld joint categories, non-destructive examination methods, and hydrostatic and pneumatic testing requirements.
This document provides information on various piping drawings used in piping design and installation. It discusses process flow diagrams (PFDs), piping and instrumentation diagrams (P&IDs), piping isometrics, plot plans, and general arrangement drawings. PFDs show the major equipment and process flows at a high level, while P&IDs provide more detailed piping information along with instrumentation and control schemes. Piping isometrics are used for fabrication and show piping runs at an angle for clarity. General arrangement drawings indicate equipment locations and piping layouts from a plan view. Together these drawings provide the necessary information for proper piping system design, installation, and operation.
Pressure Relief Systems Vol 2
Causes of Relief Situations
This Volume 2 is a guide to the qualitative identification of common causes of overpressure in process equipment. It cannot be exhaustive; the process engineer and relief systems team should look for any credible situation in addition to those given in this Part which could lead to a need for pressure relief (a relief situation).
Chris brooks storage tanks inspection, maintenance and failureSreekumar K S
API 653 tank inspections are important to identify problems and prevent tank failures. Inspections should be conducted by certified inspectors following proper protocols, including visual and ultrasound thickness testing and vacuum testing of floor seams. Tank maintenance includes regular visual inspections, keeping records, and conducting API-653 inspections every five years. Common causes of catastrophic tank failures include improper welding procedures resulting in a lack of weld fusion, not using certified welders, weld deterioration over time, overfilling tanks, and using contractors not qualified to API standards.
The document compares several pressure vessel codes and how they differ in calculating allowable stresses and vessel wall thicknesses. It finds that ASME Section VIII Division 1 is the most conservative with the highest safety factor, while the other codes allow for slightly higher stresses near the material's yield point. The codes also sometimes borrow procedures from one another, like using similar formulas for vessel heads. Overall, the document aims to explain the approaches in codes like ASME, EN, and PD5500 and how they both differ and align in designing pressure vessels.
Pressure vessels can fail due to complete rupture or leakage, resulting in dangerous consequences depending on the contained fluid. Vessels must be designed and constructed according to codes like the ASME BPVC to safely contain pressure. Common vessel types include spherical and cylindrical shapes, with cylindrical being most widely used industrially. Vessels require safety features like safety valves and inspections to prevent failure and protect people from injury. Examples of pressure vessel applications include passenger aircraft cabins, rockets, and space suits.
The document contains multiple choice questions about various engineering topics including materials, mechanics, manufacturing processes, and machinery. Each question has 4 possible answer choices labeled A-D. The questions cover topics such as V-belt speeds, material properties, steel alloys and designations, defects in castings, lubrication, heat transfer methods, combustion, and more.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for detecting various damage types affecting critical refinery infrastructure.
The document summarizes the key changes and new features in Version 4.40 of the CAESAR II pipe stress analysis software. Some of the main updates include revised piping codes, addition of the B31.11 code, expanded static load case options, automatic generation of hydrotest load cases, updates to the 3D graphics, and addition of new configuration options. The installation process for Version 4.40 is described, which includes running an installation driver from the included CD-ROM.
This Presentation is about the basic fundamentals one needs to know to begin Piping Engineering. All the basic formulas and questions that are usually asked in interviews are answered in this presentation. Feel free to ask any doubts in the comments and iI may try my best to answer them for you.
This document outlines welding standards SAES-W-010 through SAES-W-013 from Saudi Aramco. SAES-W-010 covers welding requirements for pressure vessels and discusses approved welding processes, preheat and postweld heat treatment requirements, and requirements for hardness testing and inspections. SAES-W-011 covers on-plot piping and discusses approved welding processes, weld procedures, inspections requirements and preheat/postweld heat treatment. SAES-W-012 covers pipelines and discusses approved welding processes, procedures, preheat requirements and workmanship. Finally, SAES-W-013 covers offshore structures and lists additional requirements beyond API RP-2A and AWS D1.1
Piping Training course-How to be an Expert in Pipe & Fittings for Oil & Gas c...Varun Patel
Course Description
Piping a must know skill to work in Oil & Gas and similar Process Industries.
Oil and Gas industry is become a very competitive in the current time. Getting right mentor and right exposer within industry is difficult. With limited training budget spent by company on employee training, it is difficult to acquire the knowledge to success.
Knowing cross-functional skill give you an edge over others in your career success.
This course design based on years of field experience to ensure student will comprehend technical details easily and enjoy overall journey.
Learn in detail every aspect of Pipe & Pipe Fittings used in process industry
•Different types of Pipe, Pipe fittings (Elbow, Tee, reducers, Caps etc.), Flanges, Gaskets, Branch Connection, Bolting materials
•Materials (Metal-Carbon Steel, Stainless Steel, Alloy Steel etc. Non-Metal- PVC/VCM, HDPE, GRE-GRP etc.)
•Manufacturing methods
•Heat treatment requirements
•Inspection and Testing requirements (Non Destructive Testing, Mechanical & Chemical testing)
•Dimensions & Markings requirements
•Code & Standard used in piping
Content and Overview
With 2 hours of content including 30 lectures & 8 Quizzes, this course cover every aspect of Pipe, Pipe fittings, flanges, gaskets, branch connections and bolting material used in Process Piping.
This Course is divided in three parts.
1st part of the course covers fundamental of process industries. In this Part, you will learn about fundamental process piping. You will also learn about Code, Standard & Specification used in process industries.
2nd part cover various types of material used in process industries. In this part, you will learn about Metallic and Non-Metallic material used to manufacture pipe and other piping components.
3rd parts covers in detail about pipe and piping components used in Process piping. In this part we will learn about Industry terminology of Piping components, types of industrial material grade used in manufacturing and entire manufacturing process of these components. You will learn about different manufacturing methods, Heat treatment requirements, Destructive and Non-destructive testing, Visual & Dimensional inspection and Product marking requirements.
Upon completion, you will be able to use this knowledge direct on your Job and you can easily answer any interview question on pipe & fittings.
Piping Design Course is very Important today. Basically, Piping is the work of Providing and Maintaining the Water Supply, Replacing Pipes and Pipe Work. SEA has trained & certified more than 3000 Engineers & Individuals in last five ( 5 ) years in different engineering disciplines and various sectors which include Oil and Gas , Petrochemicals , Refineries , Power Plant , Aeronautics & Construction projects etc. SEA certification / qualification is accepted and recognized by major National & International companies in the world including India , Saudi Arabia , UAE , Kuwait , Qatar , Bahrain , Oman , Jordan , Iraq , Iran , Yemen , Nigeria , Sudan , Libya , Turkey ,Portugal, Cameroon, Congo & other countries. Our SEA certified Engineers are already working in the above said countries.
Process piping fundamentals, codes and standards module 1BHARAT BELLAD
This document provides an overview of process piping fundamentals, codes, and standards. It covers topics such as pipe sizes, schedules, dimensions, materials, pressure ratings, and applicable design codes. The document is the first module in a nine-part course that introduces piping engineering concepts. It is divided into three chapters that cover piping systems basics, definitions and terminology, and relevant codes and standards like ASME B31.
This presentation describes the considerations involved in selecting the shell and tube exchanger according to TEMA Designations. Also, it helps to identify whether fluid should be sent tube side or shell side
Here's a presentation on piping engineering in PDF format, now available for all. This presentation covers the basics points of piping for our EPC industry. This presentation covers various aspects of piping engineering
Klaus P. Redmann is the Director of Quality at Disc Spring Technology, LLC. He was born in Germany and received his Masters in Chemical Engineering in 1977. His first job after university brought him to the US, where he has resided for 36 years. In addition to his role at DST, Klaus owns Redmann Quality Engineering Services, which performs quality assurance services for nuclear fuel fabrication. Klaus has extensive experience in quality systems auditing and is certified in quality engineering.
The document outlines the key engineering deliverables and responsibilities of different engineering disciplines for a project. It discusses the core deliverables and interdependencies between process, mechanical, piping, control systems, electrical, civil, structural, and architectural disciplines. Feedback from attendees is requested at the end.
This document provides standards for piping design, layout, and stress analysis. It covers topics such as design and layout considerations including numbering systems, safety, clearance, pipe routing, valves, equipment piping, and stress analysis criteria. The standards are intended to replace individual company specifications and be used in existing and future offshore oil and gas developments. It references other NORSOK and international standards and does not cover all instrument control piping, risers, sanitary piping, or GRP piping.
Safety is the most important factor in designing a process system. Some undesired conditions might happen leading to damage in a system. Control systems might be installed to prevent such conditions, but a second safety device is also needed. One kind of safety device which is commonly used in the processing industry is the relief valve. A relief valve is a type of valve to control or limit the pressure in a system by allowing the pressurised fluid to flow out from the system.
This document provides guidelines for selecting, sizing, and specifying relief devices such as pressure relief valves and rupture disks. It discusses general criteria for relief device selection, mechanical design considerations, and specific selection criteria for different services. It also covers relief device calculations, requisitioning, specifications, identification, protection, packaging, and documentation. The guidelines are based on standards from ASME, API, and ISO, and are intended to help achieve maximum technical and economic benefit from standardization when designing oil, gas, chemical, and other processing facilities.
This document provides an overview of ASME Boiler and Pressure Vessel Codes. It discusses the objectives and benefits of codes and standards, and describes the ASME Code system and some of its key sections. It focuses on introducing ASME Section VIII Division 1, covering the scope and exclusions of this section. Key topics covered include design requirements, material specifications, fabrication methods, weld joint categories, non-destructive examination methods, and hydrostatic and pneumatic testing requirements.
This document provides information on various piping drawings used in piping design and installation. It discusses process flow diagrams (PFDs), piping and instrumentation diagrams (P&IDs), piping isometrics, plot plans, and general arrangement drawings. PFDs show the major equipment and process flows at a high level, while P&IDs provide more detailed piping information along with instrumentation and control schemes. Piping isometrics are used for fabrication and show piping runs at an angle for clarity. General arrangement drawings indicate equipment locations and piping layouts from a plan view. Together these drawings provide the necessary information for proper piping system design, installation, and operation.
Pressure Relief Systems Vol 2
Causes of Relief Situations
This Volume 2 is a guide to the qualitative identification of common causes of overpressure in process equipment. It cannot be exhaustive; the process engineer and relief systems team should look for any credible situation in addition to those given in this Part which could lead to a need for pressure relief (a relief situation).
Chris brooks storage tanks inspection, maintenance and failureSreekumar K S
API 653 tank inspections are important to identify problems and prevent tank failures. Inspections should be conducted by certified inspectors following proper protocols, including visual and ultrasound thickness testing and vacuum testing of floor seams. Tank maintenance includes regular visual inspections, keeping records, and conducting API-653 inspections every five years. Common causes of catastrophic tank failures include improper welding procedures resulting in a lack of weld fusion, not using certified welders, weld deterioration over time, overfilling tanks, and using contractors not qualified to API standards.
The document compares several pressure vessel codes and how they differ in calculating allowable stresses and vessel wall thicknesses. It finds that ASME Section VIII Division 1 is the most conservative with the highest safety factor, while the other codes allow for slightly higher stresses near the material's yield point. The codes also sometimes borrow procedures from one another, like using similar formulas for vessel heads. Overall, the document aims to explain the approaches in codes like ASME, EN, and PD5500 and how they both differ and align in designing pressure vessels.
Pressure vessels can fail due to complete rupture or leakage, resulting in dangerous consequences depending on the contained fluid. Vessels must be designed and constructed according to codes like the ASME BPVC to safely contain pressure. Common vessel types include spherical and cylindrical shapes, with cylindrical being most widely used industrially. Vessels require safety features like safety valves and inspections to prevent failure and protect people from injury. Examples of pressure vessel applications include passenger aircraft cabins, rockets, and space suits.
The document contains multiple choice questions about various engineering topics including materials, mechanics, manufacturing processes, and machinery. Each question has 4 possible answer choices labeled A-D. The questions cover topics such as V-belt speeds, material properties, steel alloys and designations, defects in castings, lubrication, heat transfer methods, combustion, and more.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for detecting various damage types affecting critical refinery infrastructure.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses mechanisms like temper embrittlement, brittle fracture, thermal fatigue, erosion, corrosion under insulation, cooling water corrosion, sulfidation, chloride stress corrosion cracking, caustic stress corrosion cracking, hydrogen damage, and more. For each mechanism, it provides details on materials affected, contributing factors, inspection methods, and prevention techniques. The document is a training resource for understanding the various ways refinery equipment can deteriorate over time when exposed to different operating conditions and environments.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for detecting various damage types affecting critical refinery infrastructure.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for detecting various damage types affecting critical refinery infrastructure.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion and cracking such as temper embrittlement, brittle fracture, thermal fatigue, atmospheric corrosion, cooling water corrosion, sulfidation, chloride stress corrosion cracking, caustic stress corrosion cracking, and hydrogen damage. The key factors that influence each mechanism are described. The document emphasizes the importance of material selection, welding practices, water treatment, and inspection methods for preventing and detecting these issues.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for detecting various damage types affecting critical refinery infrastructure.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document provides an overview of various damage mechanisms that can affect fixed equipment in refineries. It discusses types of corrosion, cracking, and other material degradation processes. Some key points covered include temper embrittlement in low alloy steels, brittle fracture risks during startup and shutdown, and methods for preventing issues like thermal fatigue and caustic stress corrosion cracking. A variety of inspection techniques are also outlined for evaluating different damage mechanisms in plant equipment.
This document contains 30 multiple choice questions testing welding knowledge across various topics including welding processes, joint design, inspection methods, materials properties, and codes. The questions cover topics such as filler metal selection, essential variables requiring requalification, methods for increasing steel strength, defects that occur in parent material, and the purpose of shielding the welding arc.
1. The document contains multiple choice questions about welding processes and procedures. It covers topics like weld defects, preheat requirements, welding consumables, inspection methods, and weld quality standards.
2. Many questions relate to ensuring proper joint quality and avoiding defects like cracking or lack of fusion by following welding procedure specifications.
3. Other topics addressed include distortion control, heat input effects, and qualification testing requirements.
This is a presentation on hydrogen induced cracking ,sulfide stress cracking and test procedure for HIC resistant steel
DENZIL D’SOUZA
denzil22@gmail.com
The document summarizes hydrogen induced cracking (HIC) and sulfide stress cracking (SSC), which can occur in materials exposed to hydrogen atoms or hydrogen sulfide. It describes how cracking occurs due to hydrogen diffusion and recombination within metal lattices. Standards for testing material resistance to HIC/SSC are discussed, including test methods involving exposure to hydrogen sulfide-saturated solutions. Cracking is evaluated based on crack length and thickness ratios.
This document provides an overview of API 510 exam preparation materials covering service restrictions, joint efficiencies, and radiography requirements in ASME Section VIII. Some key points:
- Welded joints in vessels containing lethal substances must be fully radiographed and the vessel postweld heat treated if carbon/low alloy steel. Category A joints must be Type 1 (double welded) while Categories B-C can be Type 1 or 2.
- Joint categories define joint locations (e.g. longitudinal, circumferential). Type defines joint construction (e.g. double welded, single welded).
- Radiographs must show a minimum penetrameter image and identify unacceptable imperfections over certain size thresholds
1. The document provides guidance on selecting appropriate welding consumables and their properties. It lists various welding consumables for different welding processes along with their classification, applicable strength, temperature range and chemical compositions.
2. The tables show the mechanical properties and chemical compositions of different welding wires and rods for processes like GMAW, FCAW, SMAW, SAW and GTAW. Parameters like yield strength, tensile strength, impact value and applicable temperature ranges are provided.
3. Recommendations are given on the effect of postweld heat treatment and polarity on the properties and usability of different consumables. The document serves as a reference for selecting the right consumable according to the welding
DW-100 is a flux-cored wire developed nearly 30 years ago for welding mild steel and 490MPa high tensile strength steel. It has become widely used in shipbuilding and other industries due to its outstanding features such as stable arc characteristics, low spatter, self-peeling slag, high deposition rates, and consistent weld metal properties. DW-100 has maintained its reputation through quality control and remains a leader in the flux-cored wire market, accounting for about 35.5% of annual welding consumable production in Japan. It continues to be used in various applications through advanced research supporting its traditional performance.
This document discusses acceptable types of welded nozzles and other connections according to API 620. It covers reinforcement of single openings as well as spherically dished steel plate covers with bolting flanges. The document was prepared by DSc Dževad Hadžihafizović (DEng) in Sarajevo, 2023.
This document provides an overview and training on petroleum storage tanks. It discusses tank design types including fixed roof, floating roof, and pressurized storage tanks. It covers tank structure, fittings, inspection, measurement, and safety. The training outlines the goals of identifying tank types and equipment, understanding limitations, calculating volumes, and safe operation. Tank design considerations include product properties, stability calculations, and foundation types.
This document provides an overview of welding techniques including gas shielded arc welding processes like MIG/MAG and TIG welding. It discusses the principles and operation of MIG/MAG welding using solid wires and flux cored wires. For TIG welding it covers the choice of direct or alternating current, manual operation, and power sources. The document also provides welding parameters and recommendations for selecting the appropriate shielding gas for different materials.
This document discusses the different types of flanges used in piping systems. It begins by explaining what flanges are and their purpose of connecting pipes. It then describes 18 common types of flanges: weld neck, long welding neck, slip on, threaded, socket weld, lap joint, blind, orifice, nipoflange, swivel, expanding, reducing, elbow, puddle, split, cast, square, and anchor flange. Each type is defined and its typical application discussed. The document also covers common flange materials, performance features, and standards.
The document provides information about API 653 tank inspections, tank maintenance, and causes of tank failure. It discusses why tanks should be inspected, proper inspection protocols including inspector credentials, common inspection procedures, and providing calculations. It also discusses a common sense approach to tank maintenance and inspections. Finally, it outlines common causes of catastrophic tank failure such as improper welding procedures, lack of inspections, corrosion, and overfilling tanks.
The document discusses the benefits of exercise for mental health. Regular physical activity can help reduce anxiety and depression and improve mood and cognitive functioning. Exercise causes chemical changes in the brain that may help protect against mental illness and improve symptoms.
The document lists welding codes from several standards organizations, including the American Society of Mechanical Engineers (ASME), American Welding Society (AWS), American Petroleum Institute (API), Australian/New Zealand Standards, Canadian Standards Association (CSA), British Standards (BS), International Organization for Standardization (ISO), and others. It provides the organization name, titles of relevant welding standards, and brief descriptions of welding qualifications and specifications covered in each standard.
The document discusses the benefits of exercise for mental health. Regular physical activity can help reduce anxiety and depression and improve mood and cognitive functioning. Exercise causes chemical changes in the brain that may help protect against mental illness and improve symptoms.
The document discusses the benefits of exercise for mental health. Regular physical activity can help reduce anxiety and depression and improve mood and cognitive function. Exercise causes chemical changes in the brain that may help protect against mental illness and improve symptoms for those who already suffer from conditions like anxiety and depression.
This document provides information on welding techniques and materials for pipelines. It discusses manual metal arc welding as the primary process for pipeline welding. Cellulosic and basic electrodes are described as suitable filler materials. Guidelines are provided on electrode selection based on pipe steel grade and bead position. Technical data sheets specify properties of cellulosic and basic electrodes. The document also covers welding techniques, common defects, and automatic welding methods.
The document provides an overview of the typical duties of welding inspectors, which include assisting with quality control activities to ensure welded items meet specifications. Welding inspectors must understand quality control procedures and have sound welding technology knowledge. Visual inspection is a key non-destructive examination technique used by inspectors, along with other methods like surface crack detection and volumetric inspection of butt welds depending on application. Standards provide acceptance criteria for inspections, and ISO 17637 provides basic requirements for visual inspections.
This document provides concise summaries of key terms and concepts for a QC welding inspector interview. It defines common quality control terms like QA, QC, QAP, ITP, and explains the differences between them. It also summarizes welding concepts such as the four main welding types, the purpose of welding procedures like WPS and PQR, essential versus non-essential variables, and what organizations like ASME and AWS stand for.
There are numerous welding processes including arc welding, electron beam welding,
friction welding, laser welding, and resistance welding. This article will concentrate on arc
welding, which is the most common technique used to join most steels. Factors affecting
weld quality will be discussed and how to avoid common weld defects will be presented.
Arc welding requires striking a low-voltage, high-current arc between an electrode and the
base metal. The intense heat generated with this arc melts the base metal and allows the
joining of two components. The characteristic of the metal that is being welded and the joint
type (i.e. groove, fillet, etc.) dictates the welding parameters and the procedure that needs to
be followed to obtain a sound weld joint.
The document discusses the benefits of exercise for mental health. Regular physical activity can help reduce anxiety and depression and improve mood and cognitive function. Exercise causes chemical changes in the brain that may help protect against mental illness and improve symptoms.
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1. API 571 exam questions
Prepared by: DSc Dževad Hadžihafizović (DEng)
Sarajevo 2023
2. 1. A 5Cr-1Mo piping system in the hydrogen unit shows
significant internal wall loss after 2 years in service due to
CO² corrosion. Which material would be best suited to use
to install a new pipe system?
A. Titanium
B. 9Cr-1Mo
C. A-106 Gr B
D. 316 SS: D
2. A 6", A106 Gr B, flanged line carrying caustic wash water at
200°F has signs of atmospheric corrosion. Which of the
following may help accelerate the corrosion?
A. Sulfides
B. Fly ash
C. Caustic
D. None of the above: B
3. 300 Series SS, 5Cr, 9Cr, and 12Cr alloys are not susceptible
to __________ at conditions normally seen on refineries.
A. Cl SCC
B. SOHIC
C. HTHA
D. HTLA: C
4. 300 Series SS, 400 Series SS and duplex SS are subject to
pitting and localized corrosion under insulation. In addition,
__________ are also subject to SCC if chlorides are present,
while _________ are less susceptible.
A. Duplex SS, Low alloys
B. 300 Series SS, Duplex SS
C. Duplex SS, 300 Series SS
D. None of the above: B
5. 300 Series SS can be used for sour water service at
temperatures below _________, where Chloride SCC is not
likely.
A. 120°F
B. 140°F
C. 150°F
D. 175°F: B
6. 300 Series SS can suffer pitting corrosion, crevice corrosion
and ________ in fresh, blackish and salt water.
A. General corrosion
B. Oxidation
C. SCC
D. None of the above: C
7. 300 Series SS is susceptible to LME when it comes in contact
with Molten _________.
A. Cadmium
B. Mercury
C. Zinc
D. Lead: C
8. 300 Series stainless steel heater tubes in an oil-burning
furnace in the hydrocracker began to leak and the furnace
was brought down. What was the probable cause of the
cracking?
A. Chloride stress corrosion
B. Polythionic acid stress corrosion
C. Amine stress corrosion
D. Stress oriented hydrogen induced cracking.: B
9. The accepted way to test for temper embrittlement is
__________.
A. Impact testing
B. Metallographic
C. RT
D. UT shear wave: A
10. _________ acid is most often used as a catalyst in
polymerization units.
A. Polythionic
B. Naphthenic
C. Phosphoric
D. Sulfuric: C
11. All _______ based materials and low alloy materials, 300 Series
SS and 400 Series SS are susceptible Sulfidation.
A. Carbon
B. Steel
C. Chromium
D. Iron: D
12. Alloy 400 susceptible to LME when it comes on contact with
molten __________.
A. Cadmium
B. Mercury
C. Zinc
D. Lead: B
13. Alloys with increased amounts of ______ show improve
resistance to naphthenic acid corrosion.
A. Chromium
B. Molybdenum
C. Nickel
D. Carbon: B
API 571
1 / 37
3. 14. Alloys with Nickle content above ________ are highly resistant
to CI and SCC. The greatest susceptibility is 8% to 12%
nickel.
A. 15%
B. 20%
C. 30%
D. 35%: D
15. All piping and equipment exposed to HF acid at any
concentration with hardness levels above ________ are
subject to hydrogen stress cracking.
A. 200 BHN
B. 210 BHN
C. 227 BHN
D. 237 BHN: D
16. All piping and equipment exposed to HF acid at any
concentration with hardness levels above the
recommended limit (237 BHN) are subject to __________.
A. Hydrogen stress cracking
B. Sulfide stress cracking
C. Chloride stress cracking
D. None of the above: A
17. Although cracks may be seen visually, crack detection for
caustic stress corrosion cracking is best detected by WFMT,
EC, RT and ________.
A. PT
B. MT
C. ACFM
D. All of the above: C
18. Although the loss of toughness from temper embrittlement
is not evident at operating temperatures, equipment that is
temper embrittled may be susceptible to __________ during
start-up and shutdown.
A. Thermal fatigue
B. Cyclic Stress
C. Notch toughness
D. Brittle fracture: D
19. Amine corrosion depends on the design, operating
practices, the type of amine, amine concentration,
temperature and ________.
A. Pressure
B. Velocity
C. Stress
D. None of the above: B
20. Amine corrosion refers to the general and/or localized that
occurs principally on ______ in amine treating process.
Corrosion is not caused by the amine itself, but results from
dissolved acid gases (CO² and H²S), amine degradation
products, heat stable amine salts and other contaminants.
A. Carbon steel
B. Duplex SS
C. 300 Series SS
D. 400 Series SS: A
21. Amine cracking has been reported down to ambient
temperatures with some amines. ______________ temperatures
and stress levels__________ the likelihood and severity of
cracking.
A. Increasing, increases
B. Increasing, decreases
C. Decreasing, increases
D. Increasing, reduces: A
22. Amine cracking is a form of ________ stress corrosion cracking.
A. Hydrogen
B. Caustic
C. Polythionic
D. Alkaline: D
23. Amine cracking is ________ likely to occur in lean MEA and
DEA services than in MDEA and DIPA services.
A. More
B. Less
C. As
D. None of the above: A
24. Amine stress corrosion cracking is a term applied to the
cracking of steels under the combined actions of _________
and __________ in aqueous alkanolamine systems used to
remove/absorb H²S and/or CO² and their mixtures from
various gas and liquid hydrocarbon streams.
A. Temperature, pressure
B. Pressure, stress
C. Temperature, corrosion
D. Tensile stress, corrosion: D
25. Amine stress corrosion cracking is most often associated
with lean amine services. The pure alkanolamine does not
cause cracking. Cracking in rich amine services are most
often associated with _________ problems.
A. H²S
B. Stress
C. Wet H²S
D. Temperature: C
2 / 37
4. 26. Amine units are used in refineries to remove H²S, CO² and
________ from process streams originating in many units
including the coker, crude, FCC and hydrogen.
A. NA²
B. CI²
C. Mercaptans
D. None of the above: C
27. Ammonium chloride corrosion is the general or localized
corrosion, often pitting, normally occurring under
ammonium chloride or amine salt deposits. All commonly
used materials are susceptible to ammonium chloride
corrosion. A small amount of _________ can lead to very
aggressive corrosion.
A. Ammonium chloride
B. Amine
C. Water
D. Salt: C
28. Ammonium chloride salts are hydroscopic and readily
absorb water. A _________ amount of water can lead to very
aggressive ammonium chloride corrosion.
A. Large
B. Small
C. Proper
D. Improper: B
29. Ammonium chloride salts may be whitish, greenish or _______.
A. Reddish
B. Brownish
C. Yellowish
D. Bluish: B
30. The amplitude and frequency of vibration as well as the ___
of the components are critical factors in vibration-induced
fatigue.
A. Velocity
B. Temperature
C. Fatigue resistance
D. Material properties: C
31. _________ and _________ damage develop without applied or
residual stress so that PWHT will not prevent them from
occurring.
A. SOHIC, Blistering
B. SCC, SOHIC
C. HIC, SCC
D. Blistering, HIC: D
32. Annealed steels are more resistant to Spheroidization than
normalized steel. _________ grained steels are more resistant
that ________ grained steels.
A. Fine, Course
B. Course, Fine
C. PWHT, Non-PWHT
D. Non-PWHT, PWHT: B
33. Application of post-fabrication stress relieving heat
treatment of about ___________ is a proven method of
preventing carbonate cracking.
A. 1100°F
B. 1150°F
C. 1200°F
D. 1250°F: B
34. Areas of vulnerability in sulfuric acid Alkylation units
include reactor effluent lines, reboilers, deisobutanizer,
overhead systems and the _______ treating system.
A. Caustic
B. Sulfuric acid
C. Catalyst
D. H²S: A
35. ___________ are characterized by a localized loss on thickness
in the form of pits, grooves, gullies, waves, rounded holes
valleys. These losses often exhibit directional pattern.
A. Erosion
B. Corrosion/Erosion
C. Environmental corrosion
D. Both A and B: D
36. _________ are the most common type of equipment
susceptible to carburization in the refining industry.
A. Reactors
B. Heat exchanges
C. Heater tubes
D. Fin Fans: C
37. ASME Section VIII had few limitations concerning brittle
fracture prior to:
A. 1955
B. 1962
C. 1973
D. 1987: D
38. At a given pressure, the H²S concentration in the sour water
_______ as temperature _________.
A. Increases, increases
B. Decreases, decreases
C. Increases, decreases
D. Decreases, increases: D
3 / 37
5. 39. At elevated temperatures, dissimilar weld metal cracking is
aggravated by the diffusion of carbon out of weld metal
and into the base metal. The temperature at which carbon
diffusion becomes a concern is above ___________.
A. 700°F
B. 750°F
C. 800°F
D. 900°F: C
40. At elevated temperatures, the carbide phases in certain
carbon steels are unstable and may decompose into
___________. This decomposition is known as graphitization.
A. Silicon
B. Graphite nodules
C. Carbon dust
D. Graphite dust: B
41. At high temperatures, metal components can slowly and
continuously deform under load below the yield stress. This
time dependent deformation of stress components is
known as _________
A. Deformation
B. Fatigue
C. Creep
D. Thermal Fatigue: C
42. At high temperatures, metal components can slowly
continuously deform under load below the yield strength.
This time dependent deformation of stressed components
is known as ___________.
A. Creep
B. Ductility
C. Softening
D. Hardening: A
43. Atmospheric corrosion:
A. Can cause either uniform or localized wall loss
B. Always causes localized wall loss
C. Always causes uniform wall loss
D. Is best detected using profile RT: A
44. Atmospheric corrosion is of greatest concern in:
A. Dry climates in rural locations
B. Dry climates in industrial locations
C. Wet climates in rural locations
D. Wet climates in industrial locations.: D
45. The best method to inspect for SCC is _________.
A. WFMT
B. UT Shear Wave
C. AET
D. All of the above: A
46. The Best way to prevent 885°F embrittlement is to use low
____ alloys, or to avoid exposing the susceptible material to
the embrittlement range.
A. Austenite
B. Martensite
C. Ferrite
D. Chromium: C
47. The best way to prevent failures by atmospheric corrosion is
to:
A. Have an aggressive inspection program
B. Reduce airborne particles
C. Install and maintain appropriate coatings
D. Shoot all birds that cross the plant fence
E. Build new petrochemical facilities in a dry desert.: C
48. Blistering, HIC and SOHIC have been found to occur
between ambient and ________.
A. 250°F
B. 300°F
C. 350°F
D. 400°F: B
49. Blistering, HIC, SOHIC, SSC damage can occur wherever
there is a __________ environment.
A. Wet H²S
B. Hydrogen
C. Sulfur
D. Aqueous: A
50. A brittle fracture:
A. is caused by stress cycles
B. Is always the result of thermal stresses
C. Grow very rapidly with minimum deformation prior to
failure
D. Grows slowly and is dependent on time and stress.: C
51. Brittle fracture can occur during ambient temperature during
a hydro-test due to:
a. unusual loading and high toughness at the testing
temperature.
b. high impact stresses and plasticity at the testing
temperature.
c. high stresses and low toughness at the testing
temperature.
d. high strength material and temperatures below 100
degrees F.: C
52. Cadmium and lead will cause LME on ___________.
A. Copper alloys
B. 300 Series SS
C. Aluminum alloys
D. High strength steel: D
4 / 37
6. 53. Carbonate cracking typically propagates ________ to the weld;
the pattern of cracking observed on the surface is
sometimes described as _______.
A. Transverse, Eyebrow
B. Parallel, Spider web
C. Diagonal, Half moon
D. Perpendicular, Stair step: B
54. Carbonate SCC can occur at relatively low levels of _________
but usually occurs at welds that have not been stressed
relieved.
A. Residual stress
B. Applied stress
C. Acid concentration
D. Non of the above: A
55. Carbonate SCC may easily be mistaken for SCC or SOHIC;
however, the carbonate cracks are usually ________ the toe of
the weld and have multiple parallel cracks.
A. Further from
B. Closer to
C. Diagonal to
D. Perpendicular to: A
56. Carbonate stress corrosion cracking is the term applied to
surface breaking or cracks that occur adjacent to carbon
steel welds under the combined action of __________ and
_______ in carbonate containing systems.
A. Temperature, stress
B. Tensile stress, corrosion
C. Corrosion, velocity
D. Tensile stress, velocity: B
57. Carbonate stress corrosion cracking usually occurs at welds
or cold worked areas that ___________.
A. Have been stresses relieved
B. Have not been stresses relieved
C. Have high residual stress
D. Have high applied stress: C
58. Carbon dioxide (CO²) corrosion results when CO² dissolves
in water to form _________.
A. Carbon monoxide
B. Carbonic acid
C. Hydrofluoric acid
D. None of the above: B
59. Carbon dioxide corrosion results when CO² dissolves in
water to form _______ acid.
A. Sulfuric
B. Hydrochloric
C. Carbonic
D. None of the above: C
60. Carbon steel and low alloy steels are subject to excessive
hydrochloric acid corrosion when exposed to any
concentration of HCI acid that produces pH below _____.
A. 6.0
B. 5.5
C. 5.0
D. 4.5: D
61. A carbon steel bundle from the overhead condenser in the
crude unit operates at 300°F and is in hydrochloric acid
service. It showed severe pitting type corrosion when
pulled for inspection. What type of material would be best
suited for this service?
A. 5Cr-0.5Mo
B. 316 SS
C. 9Cr-1Mo
D. Titanium: D
62. Carbon steel is susceptible to SCC when used in _________
service.
A. Hydrogen
B. Ammonia
C. High temperature
D. High pressure: B
63. Carburization can be confirmed by a substantial increase
hardness and a ________ in ductility.
A. Loss
B. Gain
C. Change
D. None of the above: A
64. Carburization can be confirmed by substantial increases in
_______ and loss of _________.
A. Hardness
B. Tensile strength
C. Ductility
D. A and B
E. A and C: E
65. ___________ caustic concentrations and ________ temperature
increase the likelihood and severity f cracking with caustic
embrittlement.
A. Increasing, Decreasing
B. Decreasing, Increasing
C. Decreasing, Decreasing
D. Increasing, Increasing: D
66. Caustic embrittlement cracking can be effectively
prevented by means of PWHT at a temperature of _______.
A. 1100°F
B. 1150°F
C. 1200°F
D. 1250°F: B
5 / 37
7. 67. Caustic embrittlement is a form of ___________characterized by
surface-initiated cracks that occur in piping and equipment
exposed to caustic, primarily adjacent non-PWHT'd welds.
a. galvanic cracking
b. stress corrosion cracking
c. Chloride cracking
d. fatigue cracking: B
68. Caustic embrittlement is a form of stress corrosion cracking
characterized by surface-initiated cracks that occur in
piping and equipment exposed to caustic, primarily adjacent
to non-PWHT welds. Which of the following materials is the
most resistant to embrittlement?
A. Carbon steel
B. Nickle based alloys
C. Low alloy steels
D. 400 Series SS: B
69. Caustic is sometimes added to process streams for _________
or as a reactant.
A. Stability
B. Corrosion control
C. Neutralization
D. Inhibiting: C
70. Caustic stress corrosion cracking typically propagates
________ to the weld in adjacent base metal but can occur in
the weld deposit or heat affected zone.
A. Transverse
B. Perpendicular
C. Parallel
D. Across: C
71. Cavitation is a form of erosion by the formation and
instantaneous collapse of innumerable tiny vapor bubbles.
Temperature approaching the boiling point of the liquid are
_________ to result on bubble formation.
A. Less likely
B. More likely
C. Not likely
D. None of the above: B
72. Cavitation is best prevented by avoiding conditions that
allow the absolute pressure to fall below the _____ of the
liquid or by changing the material properties.
A. Minimum pressure
B. Pressure/Vapor ratio
C. Maximum pressure
D. Vapor pressure: D
73. Changing to a more corrosion resistant and/or higher
hardness material _______ improve cavitation resistance.
A. Will
B. May
C. Will Not
D. May Not: D
74. Characteristics stress corrosion cracks have many branches
and may be visually detectable by a _____________ appearance
on the surface.
A. Tree shaped
B. Craze-cracked
C. Multiple crack
D. None of the above: B
75. The CI SCC surface cracks appear under the action of
________, temperature and an aqueous chloride environment.
a. stagnant conditions
b. high velocity products
c. compressive stress.
d. tensile stress: D
76. Cl SCC usually occurs at metal temperatures above _________.
A. 125°F
B. 175°F
C. 140°F
D. 200°F: C
77. Components that have been carburized may have a change
in the level of _____________.
A. Carbon
B. Chromium
C. Ferromagnetism
D. Stress: C
78. Conditions favoring carburization include a high gas phase
carbon activity and ________ oxygen potential.
A. Low
B. High
C. Negative
D. Positive: A
79. A condition where steel loses strength due to the removal
of carbon and carbides leaving only an iron matrix is called
decarburization. This occurs during high temperatures,
during PWHT and from exposure to fires. Which of the
following materials is not affected by this?
A. Low alloy steel
B. Duplex SS
C. Carbon Steel
D. None of the above: B
6 / 37
8. 80. Contrary to a pure mechanical fatigue, there is no ________
load in corrosion-assistant fatigue. Corrosion promotes
failure at a lower stress and number of cycles that the
materials normal endurance.
A. Tensile
B. Stress
C. Ductile
D. Fatigue limit: D
81. Convert these temperature ---- 156°C, 450°F.
A. 304°F, 151°C
B. 284°F, 218°C
C. 312°F, 232°C
D. 296°F, 246°C: C
82. Cooling water corrosion and _________ are closely related and
should be considered together.
A. Stress
B. Velocity
C. Fouling
D. Erosion: C
83. Cooling water corrosion can result in many different forms
of damage including general corrosion, pitting corrosion,
_________, stress corrosion cracking and fouling.
A. MIC
B. HIC
C. SOHIC
D. All of the above: A
84. Cooling water corrosion is a concern with water-cooled
_________ and cooling towers in all applications across all
industries.
A. Pumps
B. Vessels
C. Piping
D. Exchangers: D
85. ___________ cooling water outlet temperatures and/or process
side outlet temperatures tend to ___________ corrosion rates
as well as fouling tendency.
A. Increasing, decrease
B. Decreasing, decrease
C. Decreasing, increase
D. Increasing, increase: D
86. Copper base alloys form sulfide at ________ than carbon steel.
a. faster rates
b. lower temperatures
c. slower rates
d. higher temperatures: B
87. Corrosion by HF (Hyrdofluoric) acid can result in high rates
of general or localized corrosion and may be accompanied
by hydrogen cracking, blistering and ________.
A. HIC
B. Delayed cracking
C. SOHIC
D. Both A and C: D
88. Corrosion due to acidic sour water containing H²S at a pH
between 4.5 and 7.0 is called sour water corrosion. Carbon
dioxide (CO²) may also be present. Which of the following
materials is susceptible to sour water corrosion?
A. Carbon Steel
B. 300 Series SS
C. 400 Series SS
D. Both B and C: A
89. Corrosion from oxygen in boiler feed water usually creates:
A. Uniform corrosion
B. Isolated pitting
C. Intergranular cracking
D. Transgranular cracking
E. Hard and brittle zones: B
90. Corrosion from oxygen tends to be _________ type damage
and can show up anywhere even if only very small amounts
break through the scavenging system.
A. General
B. Localized
C. Pitting
D. Cracking: C
91. Corrosion in boiler feedwater and condensate return
systems is usually the result of dissolved gases, oxygen and
_________.
A. Carbon monoxide
B. Carbon dioxide
C. Material properties
D. H²S: B
92. Corrosion in boiler feedwater and condensate return
systems is usually the result of dissolved gases oxygen and
________.
A. Carbon monoxide
B. H²O
C. Temperature
D. Carbon Dioxide: D
7 / 37
9. 93. Corrosion of carbon steel and other alloys from their
reaction with sulfur compounds in high temperature
environments is called _________. The presence of hydrogen
accelerates corrosion.
A. Sulfide corrosion
B. High temperature corrosion
C. H²S corrosion
D. Sulfidation: D
94. Corrosion of the anode may be significantly higher ________
to the connection to the cathode, depending on the
solution conductivity.
A. Parallel
B. Adjacent
C. Diagonally
D. Perpendicular: B
95. Corrosion protection in the boiler is accomplished by laying
down and continuously maintaining a layer of _________.
A. Manganese
B. Magnetite
C. Carbon monoxide
D. Carbonate: B
96. __________ corrosion rates are found in a gas oil desulfurizers
and hydrocrackers than naphtha desulfurizers and
hydrocrackers by a factor of almost "2".
A. Lower
B. Higher
C. Sulfidization
D. Hydrogen corrosion: B
97. Corrosion rates of the anode can be high if there is a _______
anode to cathode ratio.
A. Large
B. Small
C. Severe
D. None of the above: B
98. Corrosion rates of the anode will be less affected if there is
a _________ anode to cathode ratio.
A. Large
B. Small
C. Severe
D. None of the above: A
99. Corrosion under insulation becomes more severe at metal
temperatures between _______ and __________, where water is
likely to vaporize and insulation stays wet longer.
A. 100°C, 121°C
B. 92°C, 116°C
C. 114°C, 132°C
D. None of the above: A
100. Corrosion under insulation is more severe between _______
and _______.
A. 175°F, 212°F
B. 212°F, 350°F
C. 250°F, 300°F
D. 25°F, 250°F: B
101. Cracking and fissuring caused by HTHA are _________ and
occur adjacent to pearlite (iron carbide) areas in carbon
steels.
a. surface oriented
b. subsurface
c. laminations
d. intergranular: d
102. Cracking can occur at low caustic levels if a concentrating
mechanism is present. In such cases, caustic concentrations
of ______ ppm are sufficient to cause cracking.
A. 50-100
B. 100-150
C. 150-200
D. 200-250: A
103. _________ cracking has been a major problem in coke drum
shells.
A. Stress
B. Carburization
C. Thermal fatigue
D. Sulfide: C
104. Cracking of a metal due to stress relaxation during PWHT
or in service at elevated temperatures is called ___________. It
is most often found in heavy wall sections.
A. Thermal cracking
B. Reheat cracking
C. Step-like cracking
D. None of the above: B
105. Cracking of dissimilar weld metals occurs in the ______ side
of a weld between an austenitic and a Ferritic material
operating at high temperatures.
A. Austenitic
B. Ferritic
C. Anodic
D. Cathodic: B
106. Cracking of dissimilar weld metals occurs in the ________ side
of a weld joining 300 Series SS and carbon steel.
A. Austenitic
B. Ferritic
C. Both of the above
D. None of the above: B
8 / 37
10. 107. Cracking susceptibility increases with _______ pH and
carbonate concentration.
A. Increasing
B. Decreasing
C. Low
D. High: A
108. Cracks associated with brittle fracture will typically be
______.
A. Jagged
B. Branching
C. Straight
D. Perpendicular: C
109. Cracks connecting hydrogen blisters are referred to as
_________.
A. SOHIC
B. HIC
C. SCC
D. None of the above: B
110. Cracks that are typically straight, non-branching, and
devoid of any associated plastic deformation are likely
associated with which type of failure?
A. Stress corrosion cracking
B. Brittle fracture
C. Thermal fatigue
D. Temper embrittlement: B
111. Creep and stress rupture is more likely in a _________ grained
material than a ______ grained material.
A. Course, Fine
B. Fine, Course
C. Austenetic, Martensitic
D. None of the above: A
112. Creep damage is found in high temperature equipment
operating above the ________. Fired heater tubes and
components, Catalytic reactors, FCC reactors and FCC
fractionator and regenerator internals all operate in or
near this.
A. Transition range
B. MADT
C. Creep range
D. None of the above: C
113. The creep threshold temperature for 1¼, 2¼, 5 and 9 Cr is
__________.
A. 600°F
B. 700°F
C. 800°F
D. 1000°F: C
114. The creep threshold temperature for carbon steel is ________.
A. 315°C
B. 371°C
C. 426°C
D. 538°C: B
115. Damage due to ___________ is not visible and can only be
observed by metallographic examination.
A. Galvanic corrosion
B. Brittle fracture
C. Cavitation
D. Graphitization: D
116. Damage from sigma phase appears in the form of _______.
A. Corrosion
B. Hardness
C. Cracking
D. Ductility: C
117. Deaerator cracking problems are usually evaluated off-line
at shutdowns of boilers. What inspection method is used?
a. Radiographic inspection.
b. Wet fluorescence magnetic particle inspection.
c. Dye penetrant inspection.
d. Eddy current inspection.: B
118. Decarburization results in a ___________, which can be
confirmed by hardness testing.
A. Hardness
B. Softness
C. Brittleness
D. Oxidizing: B
119. Depending on condition of service, sulfidation corrosion is
most often in the form of:
a. random grooving.
b. uniform thinning.
c. heavy localized pitting.
d. unsystematic pitting.: B
120. Dew point corrosion can occur if the metal temperature is
below the dew point. The dew point of sulfuric acid is _______.
A. 280°F
B. 220°F
C. 310°F
D. 190°F: A
121. The dew point of hydrochloric acid depends on the
concentration of hydrogen chloride. It is typically about
_______.
A. 180°F
B. 160°F
C. 130°F
D. 110°F: C
9 / 37
11. 122. Different organisms thrive on different nutrients including
inorganic substances (Sulfur, H²S), and organic substances
(Hydrocarbons, Organic acids). In addition, all organisms
require a source of carbon, nitrogen and ____ for growth.
A. Oxygen
B. Water
C. Manganese
D. Phosphorous: D
123. Dissimilar metal welds with a 300 Series stainless steel weld
metal on a ferritic steel may also result in narrow region of
_______ at the toe of the weld, near the fusion line on the
ferritic side.
A. Ductility
B. Hardness
C. Cracking
D. None of the above: B
124. Dissimilar weld metal cracking can be aggravated by
_________.
A. Stress
B. Pressure
C. Thermal cycling
D. Cyclic stresses: C
125. Dissimilar weld metal cracking forms at the toe of the weld
in the heat affected zone of the _______ material.
A. Ferritic
B. Austenitic
C. Martensitic
D. Both B and C: A
126. Dissimilar weld metal cracking occurs because the
coefficients of thermal expansion between ferritic steel
and 300 Series stainless steels differ by ______ or more.
A. 10%
B. 15%
C. 20%
D. 30%: D
127. The effects of hydrogen embrittlement __________ with
_________ temperatures.
A. Increase, increasing
B. Decrease, decreasing
C. Increase, decreasing
D. Decrease, increasing: D
128. __________ eliminates the susceptibility of most common
steels to SCC.
A. Preheat
B. High temperature
C. PWHT
D. All of the above: C
129. The endurance limit is usually about:
A. 10-20% of a material's ultimate tensile strength
B. 40-50% of a material's ultimate tensile strength
C. 10-20% of a material's yield strength
D. 40-50% of a material's yield strength: B
130. Equipment that is exposed to moving fluids and/or catalyst
are subject to erosion and erosion-corrosion.
What unit is most often damaged by gas borne catalyst
particles?
a. Desalting Unit.
b. Motor Oil Unit.
c. Crude and Vacuum Unit.
d. Fluid Catalytic Cracker.: D
131. Equipment that is temper embrittled may be susceptible to
_________ during start-up and shutdown.
A. Creep
B. Thermal fatigue
C. Brittle fracture
D. Stress fatigue: C
132. Erosion-corrosion is a description for the damage that
occurs when corrosion contributes to erosion by removing
protective films or scales, or by exposing the metal surface
to further ________ under the combined action of corrosion-
erosion.
A. Stress
B. Corrosion
C. Oxidation
D. None of the above: B
133. Erosion-corrosion is best controlled by using __________
and/or altering the process environment to reduce
corrosivity.
a. corrosion inhibitors
b. wear plates
c. hard-facing by weld overlays
d. more corrosion-resistant alloys: D
134. Exposure to high solution caustic can result in general
corrosion or high corrosion rates above ___________.
A. 175°F
B. 150°F
C. 125°F
D. 100°F: B
135. The extent and depth of decarburization is a function of
temperature and ________.
A. Pressure
B. Material properties
C. Exposure Time
D. Velocity: C
10 / 37
12. 136. Fatigue cracks usually initiate on the surface at notches or
___________ under cyclic loading.
A. Branches
B. Laterals
C. Stress concentrations
D. Grinding marks: C
137. A fatigue failure exhibits what type of "fingerprint" or
appearance?
a. The failure exhibits a hash mark type of fingerprint that
radiates from the crack origin.
b. The failure exhibits a "clam shell" type of fingerprint that
has concentric rings called "beach marks" .
c. The failure exhibits a wavy type of fingerprint that is
random in nature.
d. The failure exhibits a ragged rough type of fingerprint
that emanates from the failure point.: B
138. A fatigue fracture is brittle and the cracks are most often
________.
A. Parallel
B. Transgranular
C. Intergranular
D. Transverse: B
139. Fatigue will not occur in carbon steel if stresses are below
the:
A. Transition limit
B. Endurance limit
C. Hardening limit
D. Speed limit: B
140. Ferritic stainless steels are usually not used in ________
applications.
A. Non-pressure boundary
B. Pressure boundary
C. High temperature
D. Low temperature: B
141. For 5Cr-0.5Mo, what is the threshold temperature for creep?
A. 500°F
B. 800°F
C. 600°F
D. 700°F: B
142. For a specific material, HTHA is dependent on temperature,
hydrogen partial pressure, time and _____________.
A. Stress
B. Pressure
C. Velocity
D. Alloy composition: A
143. For carbon steel, common velocity limits are generally
limited to ________ fps for rich amine and _________fps for lean
amine.
A. 8-10, 30
B. 6-9, 15
C. 4-8, 10
D. 3-6, 20: D
144. For furnaces, to prevent PASCC, keep the firebox heated
above the dew point to keep _________ from forming.
A. Water
B. Acids
C. Moisture
D. Corrosion: B
145. For galvanic corrosion to take place, three condition must
met, presence of an electrolyte, two different materials or
alloys and _________.
A. a cathode
B. a anode
C. an electrical connection
D. None of the above: C
146. Formation of a metallurgical phase known as sigma phase
results in a loss of ________ in some stainless steels as a
result of high temperature exposure.
A. Ductility
B. Fracture toughness
C. Embrittlement
D. None of the above: B
147. Formation of sigma phase in austenitic stainless steels can
also occur in a few hours, as evidenced
by the known tendency for sigma to form if an austenitic
stainless steel is subjected to a post weld
heat treatment at _______.
A. 1150°F
B. 1275°F
C. 1100°F
D. 1325°F: B
148. A form of corrosion caused by living organism such as
bacteria, algea or fungi is ___________.
A. HIC
B. SOHIC
C. MIC
D. None of the above: C
11 / 37
13. 149. A form of corrosion that can occur at the junction of
dissimilar metals when they are joined together in a suitable
electrolyte is _______.
A. Galvanic corrosion
B. Anodic corrosion
C. Cathodic corrosion
D. All of the above: A
150. A form of fatigue cracking in which cracks develop under
the combined effects of cyclic loading and corrosion is
called _________. Cracking often initiates at stress
concentrations such as a pit in the surface.
A. Cyclic cracking
B. Corrosion cracking
C. Stress fatigue
D. Stress cracking: B
151. A form of mechanical fatigue in which cracks are produced
as a result of dynamic loadings is ________.
A. Spheroidization
B. Vibration-induced cracking
C. Fatigue cracking
D. Stress cracking: B
152. A form of thermal cracking, _________, can occur when high
nonuniform thermal stresses develop over a relatively short
period of time in a piece of equipment due to differential
expansion and contraction.
A. Thermal expansion
B. Thermal stress
C. Thermal shock
D. Linear expansion: C
153. For pressure vessels, inspection should focus on welds of
________ operating in the creep range.
A. CrMo alloys
B. Carbon steel
C. Stainless steel
D. Low hydrogen electrodes: A
154. For some materials such as titanium, carbon steel and low
alloy steel, the number of cycles to fatigue fracture
decreases with __________ until an endurance limit is reached.
Below this endurance limit, fatigue cracking will not occur,
regardless of the number of cycles.
A. Temperature increases
B. Stress amplitude
C. Pressure decreases
D None of the above: B
155. Foul smelling water may be sign of fouling and/or ________.
A. MIC
B. HIC
C. SOHIC
D. All of the above: A
156. Galvanized steel components should not be welded to
_______ due to LME.
A. 300 Series SS
B. 400 Series SS
C. Carbon Steel
D. Duplex SS: A
157. General or localized corrosion of carbon steels and other
metals caused by dissolved salts, gases, organic compounds
or microbiological activities is called_______.
A. Flue Gas Corrosion
B. Atmospheric corrosion
C. Cooling water corrosion
D. None of the above
E. All of the above: C
158. General or localized corrosion of carbon steels and other
metals caused by dissolved salts, gases, organic compounds
or microbiological activity is called ______.
A. Cooling water corrosion
B. Oxidation
C. MIC
D. None of the above: A
159. Geometry, stress level, _________ and material properties are
the predominate factors in determining the fatigue
resistance of a component.
A. Temperature
B. Pressure
C. Velocity
D. Number of cycles: D
160. Geometry, stress level, number of cycles and ________ are
the predominate factors in determining the fatigue
resistance of a component.
A. Temperature
B. Material properties
C. Pressure
D. Velocity: B
12 / 37
14. 161. The grain size has an important influence on the high
temperature ductility and on the reheat cracking
susceptibility. A ___________ grain size results in ________ ductile
heat affected zones, making the material more susceptible
to reheat cracking.
A. Large, more
B. Small, less
C. Large, less
D. Small, more: C
162. Graphitization can be prevented by using chromium
containing low alloys steels for long-term exposure above
__________.
A. 650°F
B. 700°F
C. 750°F
D. 800°F: D
163. The graphitization rate ___________ with increasing
temperature.
A. Increases
B. Decreases
C. Stops
D. Proceeds: A
164. ________ greatly increase the probability and severity of
blistering, HIC and SOHIC damage.
A. Acids
B. Caustics
C. Amines
D. Cyanides: D
165. A hard, brittle surface layer will develop on some alloys
due to exposure to high temperature process streams
containing high levels of nitrogen compounds such as
ammonia or cyanides, particularly under reducing
conditions, is called _________.
A. Carburization
B. Spheroidization
C. Nitriding
D. None of the above: C
166. Hardness is primarily an issue with SSC. Typical low
strength carbon steel should be controlled to produce
weld hardness less than _________.
A. 225 BHN
B. 237 BHN
C. 200 BHN
D. 240 BHN: C
167. Hardness levels above _________ are highly susceptible to
hydrogen stress cracking (HF). Time-to-failure decreases as
the hardness increases.
A. 225 BHN
B. 237 BHN
C. 241 BHN
D. 247 BHN: B
168. ____________ has been a major problem on coke drum shells.
A. Thermal fatigue
B. Stress cracking
C. Erosion
D. Temper embrittlement: A
169. HCl acid corrosion is found in several units, especially _______
and _________ units, hydroprocessing units and catalytic
reformer units.
A. Amine, crude
B. Crude, Alkylation
C. Vacuum, Amine
D. Crude, Vacuum: D
170. Heat treatment can have a significant effect on the
toughness and hence fatigue resistance of a metal. In
general, _________ grained microstructures tend to perform
better then _________ grained.
A. Fine, Course
B. Austenetic, Martensitic
C. Course, Fine
D. Martensitic, Austenetic: A
171. Higher _________ containing alloys are used for improved
resistance to naphthenic acid corrosion.
A. Chromium
B. Carbon
C. Molybdenum
D. All of the above: C
172. High strength, low alloy steels such as A193-B7 bolts and
compressor parts are susceptible to hydrogen stress
cracking. A193-B7M Bolts are susceptible if __________.
A. Exposed
B. Overtorqued
C. Double nutted
D. None of the above: B
173. High strength steels are susceptible to LME when they
come in contact with molten ___________.
A. Cadmium
B. Zinc
C. Lead
D. Both A and C: D
13 / 37
15. 174. High temperature H² / H²S corrosion damage is minimized
by using alloys with high ___________ content.
A. Carbon
B. Molybdenum
C. Chromium
D. Stainless: C
175. High temperature hydrogen attack results from exposure to
hydrogen at elevated temperature and pressures. The
hydrogen react with _________ in steel to produce _______,
which cannot diffuse through steel. The loss of carbides
causes an overall loss in strength.
A. Carbides, oxygen
B. Alloys, hydrogen dioxide
C. Carbides, methane
D. Hydrogen dioxide, H²S: C
176. How do you mitigate brittle fracture of new equipment.
a. Use only 400 series stainless steels.
b. Use only 300 series stainless steels.
c. Use material specifically designed for low temperature
operation per ASME B&PV Code.
d. Use material designed for high temperature operation
per ASME B&PV Code.: C
177. How is the effectiveness of treatment monitored in cooling
water systems?
a. using AE.
b. measuring biocide residuals.
c. using velocity ratio technique.
d. using ACFM technique.: B
178. How many mils per year would you expect a carbon steel
line to lose if exposed to a marine environment?
a. 20 mpy
b. 15 mpy
c. 10 mpy
d. 5 mpy: A
179. HTHA is dependent on temperature, hydrogen partial
pressure, time and ________.
A. Pressure
B. Stress
C. Yield
D. Tensile strength: B
180. Hydriding of titanium is a metallurgical phenonemon in
which hydrogen diffuses into the titanium and reacts to
form an embrittling phase. This can results in a complete
loss of ________ with no noticeable sign of corrosion or loss
of thickness.
A. Strength
B. Ductility
C. Carbides
D. Hardness: B
181. Hydrochloric acid corrosion is a general and localized
corrosion and is very aggressive to most common materials
on construction. Damage in refineries is often associated
with dew point corrosion in which vapors containing _______
and hydrogen chloride condense from the overhead stream
of a distillation, fractionation, or stripping tower.
A. O²
B. O
C. H²O
D. CO²: C
182. Hydrogen blisters may form as surface bulges on the ID,
the OD on within the wall thickness of a pipe or pressure
vessel. Blistering occurs from hydrogen generated by
__________, not hydrogen gas from the process stream.
A. H²S
B. Corrosion
C. Hydriding
D. Sulfur: B
183. Hydrogen blisters may form at many different depths from
the surface of the steel, in the middle of the plate or near a
weld. In some cases, neighboring or adjacent blisters that
are at slightly different depths (planes) may develop cracks
that link them together. Interconnecting cracks between
the blisters often have a ________ appearance.
A. Crescent
B. Eyebrow
C. Step Like
D. Jagged: C
184. Hydrogen permeation or diffusion rates have been found to
be minimal at pH __________ and increase at both higher and
lower pH's.
A. 4
B. 5
C. 6
D. 7: D
185. Hydrogen stress cracking is the same mechanism that is
responsible for sulfide stress corrosion cracking in wet H²S
environments except that HF acid is generating the ________.
A. Sulfide
B. Caustic
C. Hydrogen
D. Water: C
186. Hydrogen stress cracking is the same mechanism that is
responsible for sulfide stress corrosion cracking in wet H²S
environments except that HF acid is generating the ________.
A. Sulfide
B. Corrosion
C. Hydrogen
D. None of the above: C
14 / 37
16. 187. If the BHN is 400-500 it may indicate __________.
A. Carburization
B. Hydriding
C. Temper embrittlement
D. Caustic embrittlement: B
188. If weld repairs are required, the effects of temper
embrittlement can be temporarily reversed (de-embrittled)
by heating at __________ for 2 hours per inch of thickness and
rapidly cooling to room temperature.
A. 1000°F
B. 1150°F
C. 1200°F
D. 1250°F: B
189. If wet electrodes or high moisture content flux is used,
___________ can be charged into the steel resulting in delayed
cracking.
A. Atomic hydrogen
B. Hydrogen
C. Oxygen
D. H²O: B
190. If wet electrodes or high moisture content flux weld
electrodes are used to weld carbon steel, hydrogen can be
charged into steel resulting in ________________.
A. Reduced tensile strength
B. Loss of ductility
C. Delayed cracking
D. All of the above: C
191. Improved resistance to erosion is usually achieved through
increasing substrate ________ using harder alloys, hard facing
or face-hardening treatment.
A. Composition
B. Stress
C. Hardness
D. None of the above: C
192. In a pump, the difference between the actual pressure, or
head, of a liquid available (measured on the suction side)
and the vapor pressure of that liquid is called Net Positive
Suction Head (NPSH) available. The minimum head required
to prevent cavitation with given liquid at a given flow rate is
called Net Positive Suction Head _________. Inadequate NPSH
can result in cavitation.
A. Surplus
B. Required
C. Reserve
D. None of the above: B
193. Increasing chromium content in the alloy improves
resistance to sulfidation. However, there is little
improvement with increasing chromium content until about
______ Cr.
A. 3-5
B. 5-7
C. 7-9
D. 9-12: C
194. Increasing the chromium in steels offers no major
improvement in resistance to CO² corrosion until a minimum
of _________ is reached.
A. 9%
B. 12%
C. 5%
D. 7%: B
195. In design and fabrication, it is advisable to avoid sharp
changes in cross section, such as short radius fillets or
undercut that can give rise to _________.
Long-seam welds are particularly susceptible to reheat
cracking due to mismatch caused by fit up problems.
A. Stress concentrations
B. Cracking
C. Circumferential stress
D. All of the above: A
196. In fired heater tubes, dissimilar weld metal cracking forms
primarily on the _________ of the material.
A. Outside
B. Inside
C. Welds
D. All of the above: A
197. In general, the resistance of carbon steel and other alloys
to high temperature corrosion is determined by the ________
content of the material.
A. Molybdenum
B. Chromium
C. Carbon
D. All of the above: B
198. In general, the resistance of iron and nickel based alloys to
sulfidation is determined by the _________ content of the
material.
A. Chromium
B. Carbon
C. Molybdenum
D. Alloying: A
15 / 37
17. 199. In HF Service, carbon steel form a protective _______ scale in
dry concentrated acid. Loss of the protective scale through
high velocities or turbulence will result in greatly
accelerated corrosion rates.
A. Chloride
B. Fluoride
C. Iron sulfide
D. Iron oxide: B
200. In HF service, carbon steel forms a protective fluoride
scale in dry concentrated acid. Loss of the protective scale
through high _________ or turbulence will result in greatly
accelerated corrosion rates.
A. Temperature
B. Pressure
C. Velocities
D. None of the above: C
201. In HF service, carbon steel operating above ________ should
be closely monitored for loss on thickness and may need
to be upgraded to Alloy 400.
A. 150°F
B. 175°F
C. 160°F
D. 200°F: A
202. ___________ injection downstream of the desalter is another
common method used to reduce the amount of HCl going
overhead.
A. Hydrogen
B. Nitrogen
C. Water
D. Caustic: D
203. In most cases, brittle fracture occurs only at temperatures
below the Charpy impact _______________ temperature, the
point at which the toughness of the material drops off
sharply.
a. failure
b. transition
c. critical
d. stable: B
204. In most cases, brittle fracture occurs only at temperatures
below the Charpy impact transition temperature. Steel
cleanliness and __________ have a significant influence on
toughness and resistance to brittle fracture.
A. Alloy composition
B. Tensile strength
C. Grain Size
D. Pressure: C
205. In most cases, brittle fracture occurs only at temperatures
________ the Charpy impact transition temperature.
A. Above
B. Below
C. Around
D. Inside: B
206. In order for PASCC to occur the material must be ___________.
A. PWHT
B. Non-PWHT
C. Sensitized
D. Austenetic: C
207. In order to minimize and prevent amine SCC, PWHT all
carbon steel welds in accordance with API RP _________.
A. 751
B. 912
C. 510
D. 945: D
208. In piping and equipment, creep cracking can occur where
high metal temperatures and _________ occur together. Creep
cracking, once initiated, can progress rapidly.
A. Pressures
B. Stress risers
C. Velocities
D. None of the above: B
209. In pressure containing equipment, SOHIC and SCC damage
is most often associated with ________.
A. Internals
B. Weldments
C. Branches
D. None of the above: B
210. Inspecting for high-cycle fatigue can be difficult since:
A. The cracks are extremely tight
B. Predicting the location of cracking is difficult
C. Once the crack begins, only a few cycles are needed for
the crack to lead to failure.
D. Often the equipment is vibrating making non-destructive
evaluations difficult.: C
211. Inspection for wet H²S damage generally focuses on ________
and _______.
A. Weld seams, Nozzles
B. Trays, Weld Seams
C. Nozzles, trays
D.None of the above: A
16 / 37
18. 212. An inspector notes that there are cracks in the brick
fireproofing of a column supporting a vessel on a FCC unit.
An inspection hole is opened to check the condition of the
column. Heavy rust scale is present and the inspector
requires the entire column to be stripped. Severe pitting to
holes and serious thinning of the column is found. What
type of corrosion would this be?
a. Heavy erosion from catalyst.
b. Chloride attack.
c. Normal weathering of the column.
d. CUI (corrosion under insulation).: D
213. In susceptible materials, Primary factor that affects sigma
phase formation is the ___________ at elevated temperatures.
A. Time of exposure
B. Pressure
C. Stress
D. Velocity: A
214. In vessels and piping, creep cracking can occur where high
metal temperatures and ________ occur together.
A. Pressures
B. Stress Concentrations
C. Velocities
D. None of the above: B
215. In what type of environment would atmospheric corrosion
be most severe?
a. Marine environments, and moist polluted industrial
environments.
b. Desert environments, and cold dry rural environments.
c. Areas exposed to the morning sun and prevailing winds.
d. Far north environments with maximum exposure to cold
and snow.: A
216. __________ is accelerated high temperature wastage of
materials that occurs when contaminants in the fuel form
deposits and melt on the metal surfaces.
A. Spheroidization
B. Dealloying
C. Fuel ash corrosion
D. None of the above: C
217. ____________ is a change in the microstructure of certain
carbon steels and 0.5 Mo steels after long term operation
in the 800°F to 1100°F range.
A. Graphitization
B. Softening
C. Temper Embrittlement
D. Creep: A
218. _____________ is a change in the microstructure of certain
carbon steels and 0.5Mo steels after long-term operation
in the 800°F to 1100°F range that may cause a loss in
strength, ductility and/or creep resistance.
A. Embrittlement
B. Carburization
C. Graphitization
D. Sensitization: C
219. ___________ is a change on the microstructure of steels after
exposure in the 850°F to 1400°F range, where the carbide
phases in carbon steels are unstable and may agglomerate
from their normal plate-like appearance.
A. Carburization
B. Spheroidization
C. Graphiding
D. 885°F embrittlement: B
220. ________ is a form of carbon that may promote carburization,
particularly during decoke cycles where temperatures
exceed the normal operating temperatures.
A. Carbonic acid
B. Coke
C. Crude oil
D. None of the above: B
221. ___________ is a form of carburization resulting in accelerated
localized pitting which occurs in carburizing gases and/or
process streams containing carbon and hydrogen. Pits
usually form on the surface and may contain soot or
graphite dust.
A. Hydrate corrosion
B. Carbide corrosion
C. Spheroidization
D. Metal dusting: D
222. ___________ is a form of cracking that results when certain
molten metals come in contact with specific alloys.
Cracking can be very sudden and brittle in nature.
A. SCC
B. LME
C. AET
D. SOHIC: B
223. ___________ is a form of damage found mostly in older vintage
carbon steels and C-0.5 Mo low alloy steels under the
combined effects of deformation and aging at an
intermediate temperature.
A. Spheroidization
B. Thermal fatigue
C. Strain aging
D. None of the above.: C
17 / 37
19. 224. _______________ is a form of environmental cracking that can
initiate on the surface of high strength low alloy steel and
carbon steels with highly localized zones of high hardness
on the weld metal and HAZ as a result of exposure to
aqueous HF acid service.
A. Sulfide stress cracking
B. Hydrogen stress cracking
C. Caustic stress cracking
D. Hydrogen induced cracking: B
225. ___________ is a form of stress corrosion cracking normally
occurring during shutdowns, startups or during operation
when air and moisture are present. Cracking is due to sulfur
acids forming from sulfide scale, air and moisture on
sensitized stainless steel.
A. Caustic SCC
B. Chloride SCC
C. Polythionic acid SCC
D. None of the above: C
226. _____________ is a form or erosion caused by the formation
and instantaneous collapse of innumerable tiny vapor
bubbles.
A. Condensate corrosion
B. Cavitation
C. Dew-point corrosion
D. Atmospheric corrosion: B
227. _________ is a loss in toughness due to metallurgical change
that can occur in alloys containing a ferrite phase, as a
result of exposure in the temperature range 600°F to
1000°F.
A. Caustic embrittlement
B. Notch toughness
C. 885°F embrittlement
D. Ductile embrittlement: C
228. ____________ is a mechanical form of degradation that occurs
when a component is exposed to cyclical stresses for a
extended period, often resulting in sudden unexpected
failure.
A. Stress fatigue
B. Mechanical fatigue
C. Thermal fatigue
D. Cyclic fatigue.: B
229. ___________ is a selective corrosion mechanism in which one or
more constituents of an alloy are preferentially attacked
leaving a lower density often porous structure.
A. Phenol corrosion
B. Dealloying
C. Carburization
D. Preferentially weld attack: B
230. __________ is most likely found in hard welds and heat
affected zones and in high strength components.
A. SOHIC
B. HIC
C. Carburization
D. SSC: D
231. ____________ is most likely found on hard weld and heat-
affected zones and in high strength components.
A. HIC
B. SSC
C. SOHIC
D. Blistering: B
232. ___________ is often found in piping and equipment that
handles caustic, including H²S and mercaptan removal units,
as well as equipment that handles caustic, including H²S and
mercaptan removal unit, as well as equipment that uses
caustic for neutralization in sulfuric acid and HF acid units.
A. Carburization
B. Sulfide corrosion
C. Caustic embrittlement
D. Hydrogen cracking: C
233. ____________ is similar to HIC but is a potentially more
damaging form of cracking which appears as arrays of
cracks stacked on top of each other. The result is a through
thickness crack that is perpendicular to the surface and is
driven by high levels of stress.
A. MIC
B. SOHIC
C. Sulfuric SCC
D. None of the above: B
234. ___________ is surface initiated cracks caused by
environmental cracking of 300 Series SS and some nickel
based alloys under the combined action of tensile stress,
temperature and aqueous chloride environment. The
presence of dissolved oxygen increases the propensity for
cracking.
A. SSC
B. SOHIC
C. CI SCC
D. HIC: C
235. ___________ is the main concern during start-up, shutdown
and/or hydro testing for equipment/piping operating at
elevated temperatures. This event can also occur in an auto
refrigeration event in units processing light hydrocarbons.
A. Stress fracture
B. Carburization
C. Spheroidization
D. Brittle fracture: D
18 / 37
20. 236. ___________ is the primary alloying agent that affects
resistance to oxidation.
A. Chromium
B. Molybdenum
C. Silicon
D. Aluminum: A
237. ________ is the reduction in toughness due to metallurgical
change that can occur in some low alloy steel as a result of
long-term exposure in the temperature range of about
650°F to 1100°F.
A. Hardening
B. Graphitization
C. Spheroidization
D. Temper embrittlement: D
238. _________ is the result of cyclic stress caused by variation in
temperature.
A. Creep
B. Thermal fatigue
C. Cyclic cracking
D. Stress corrosion cracking: B
239. ___________ is the result of cyclic stresses caused by variation
in temperature.
A. Cyclic cracking
B. Stress cracking
C. Stress fatigue
D. Thermal fatigue: D
240. ______ is the sudden rapid fracture under stress (residual or
applied) where the material exhibits little or no evidence of
ductility or plastic deformation.
A. Thermal fatigue
B. Thermal shock
C. Brittle fracture
D. Stress fracture: C
241. _________ is usually found in aqueous environments or
services where water is sometimes or always present,
especially where stagnant or low-flow conditions allow the
growth of microorganisms.
A. MIC
B. HIC
C. SOHIC
D. None of the above: A
242. ___________ is when oxygen reacts with carbon steel and
other alloys at high temperature converting the metal to
oxide scale.
A. High temperature corrosion
B. Oxidation
C. Dealloying
D. Thermal fatigue: B
243. It is generally accepted that stresses approaching _________
are required for SCC to occur so that thermal stress relief is
effective in preventing caustic SCC.
A. MAWP
B. Yield
C. Creep range
D. Critical: B
244. Key factors affecting thermal fatigue are the magnitude of
the_______________ and the ____________.
a. temperature; rate (speed of rise)
b. equipment size; complexity (intricacy of construction)
c. stress loading; size (increase, decrease of loads)
d. temperature swing; frequency (number of cycles): D
245. Key factors affecting thermal fatigue are the magnitude of
the temperature and the _________.
A. Number of cycles
B. Pressure
C. Stress
D. Alloy composition: A
246. Lean amine is generally not corrosive because they either
have low conductivity and/or high pH. Corrosion rates
increase with increasing temperature, particularly in rich
amine service. Temperatures above ___________ can result in
acid gas flashing and severe localized corrosion.
A. 170°F
B. 190°F
C. 220°F
D. 240°F: C
247. The level of creep damage is a function of the material and
the coincident _______ level at which the creep deformation
occurs.
A. Pressure/Temperature
B. Pressure/Stress
C. Temperature/Stress
D. None of the above: C
248. The "L" grade of stainless steel will sensitize if exposed
more than several hours above _________ or long term above
_________.
A. 1200°F, 800°F
B. 1000°F, 600°F
C. 1000°F, 750°F
D. 1100°F, 800°F: C
249. Liquid metal embrittlement can occur if 300 Series SS
comes in contact with molten __________.
A. Copper
B. Mercury
C. Zinc
D. Lead: C
19 / 37
21. 250. Localized corrosion due to the concentration of caustic or
alkaline salts that usually occurs under evaporative
conditions is ____________.
A. Carbonate corrosion
B. Caustic corrosion
C. Alkaline Corrosion
D. None of the above: B
251. A loss in ductility of high steels due to penetration of
atomic hydrogen can lead to brittle cracking hydrogen
embrittlement. Which of the following materials is
susceptible to HE.
A. Carbon Steel
B. 400 Series SS
C. low alloy steel
D. All of the above: D
252. The loss in strength from spheroidization (Softening) is
usually accompanied by a(n) _________ in ductility, which
allows for deformation at stress concentration.
A. Increase
B. Decrease
C. Reduction
D. Yield: A
253. Low alloy steels contain a maximum of ______ chrome.
A. 5%
B. 6%
C. 7.5%
D. 9%: D
254. Low Creep ductility is ______ prevalent at the lower
temperatures in the creep range. Or low stresses in the
upper creep range.
A. More
B. Less
C. Equally
D. None of the above: A
255. Low creep ductility is _________ severe in high tensile
strength materials and welds.
A. More
B. Less
C. Usually
D. Not: A
256. The major factors affecting high temperature sulfidation are
the temperature, the presence of hydrogen, the
concentration of H²S and the __________.
A. Alloy content
B. Velocity
C. Pressure
D. Water content: A
257. The major factors affecting high temperature sulfidation are
the temperature, the presence of hydrogen, the H²S
concentration and the _________.
A. Pressure
B. Stress
C. Alloy composition
D. Velocity: C
258. Major factors affecting sulfidation are alloy composition,
temperature and _________.
A. Time
B. Stress
C. Concentration of hydrogen
D. Concentration of Sulfur: D
259. Major factors affecting sulfidation are alloy composition,
temperature and concentration of _________ corrosive
compounds.
a.water
b. hydrogen
c. sulfur
d. ammonia: C
260. Many thermal fatigue cracks are filled with:
A. chlorides
B. hydroslime
C. oxides
D. sulfides: C
261. ________ material sections also have a ________ resistance to
brittle fracture due to higher constraint, which increases
triaxial stresses at the crack tip.
A. Thinner, lower
B. Thicker, Lower
C. Thinner, Higher
D. Thicker, Higher: B
262. Mechanical fatigue can cause cracks that initiate from the
surface and often form a:
A. Clam shell appearance
B. Snail shell appearance
C. Turtle shell appearance
D. None of the above: A
263. Mechanical fatigue is caused by:
A. cyclic stresses occurring over a long period of time
B. Higher than average stresses at high temperatures
C. Constant stresses occurring at low temperatures
D. Cyclic operating conditions of bird poop, then rain etc.: A
20 / 37
22. 264. Metal dusting is preceded by ________ and is characterized
by rapid metal wastage.
A. Decarburization
B. Carburization
C. Graphitization
D. None of the above: B
265. Metallic components form a surface _________ when exposed
to sulfur compounds. This may react with air (oxygen) and
moisture to form sulfur acids (polythionic acid).
A. Oxide
B. Sulfide scale
C. Sulfate scale
D. Caustic scale: B
266. MIC is often characterized by _________ within pits in carbon
steel.
A. Oxide
B. Tubercles
C. Worm Holes
D. Cup shaped pits: D
267. MIC is often found in _________, bottom water storage tanks,
piping with stagnant or low flow and piping in contact with
some soils.
A. Vessels
B. Heat exchangers
C. Drums
D. All of the above: B
268. A minimum of ________ to _______ molybdenum is needed in
alloy to resist naphthenic acid corrosion.
A. 2%, 3%
B. 1½%, 2½%
C. 2%, 2½%
D. 1%, 2%: C
269. Mitigation of CUI is best achieved by __________.
A. A properly documented inspection program.
B. A properly installed insulation system.
C. A properly applied coating system
D. A properly documented NDE program.: C
270. The more noble material, called the __________, is protected
by sacrificial corrosion of the more active material, called
____________. The more active metal corrodes at a higher rate
than it would if it were not connected tot he more noble
metal.
A. Anode, Cathode
B. Cathode, Anode
C. Alpha, Omega
D. None of the above: B
271. Most brittle failures appear as:
A. Branched cracking
B. Intergranular cracking
C. Ductile tears
D. Cleavage: D
272. Most Brittle failures occur:
A. Below the impact transition temperature
B. On thinner materials
C. On "Clean" steel
D. While in operation at elevated temperatures: A
273. The most common method used for monitoring
underground structures is measuring the structure to soil
__________ using dedicated reference electrodes near the
structure.
A. Resistivity
B. Corrosiveness
C. Potential
D. Electrolyte: C
274. The most important factors affecting graphitization are the
chemistry, stress, temperature and ______.
A. Velocity
B. Time at exposure
C. Pressure
D. Ductility: B
275. NAC may be found in hot hydrocarbon streams downstream
of the crude and vacuum units, ___________ any hydrogen mix
point.
A. Upstream of
B. Downstream of
C. Adjacent to
D. Around: A
276. Naphthenic acid corrosion is a form of high temperature
corrosion that occurs primarily in crude and vacuum units
and downstream units that process certain fractions that
contain naphthenic acid. Which of the following materials is
susceptible to naphthenic acid corrosion?
A. Carbon steel
B. 300 Series SS
C. 400 Series SS
D. All of the above: D
277. Naphthenic acid corrosion is most severe in __________ flow;
in areas of high velocity or turbulence and in distillation
towers where hot vapors condense to form liquid droplets.
A. Single phase
B. Two phase
C. Three phase
D. Negative phase: B
21 / 37
23. 278. Naphthenic acid is ______ by catalytic reactions on
downstream hydro processing and FCC units.
A. Enhanced
B. Destroyed
C. Concentrated
D. Diluted: B
279. Nickel based alloys usually contain _______ nickel.
A. >30%
B. >20%
C. >10%
D. >12%: A
280. Nitriding begins above _________ and becomes severe above
________.
A. 500°F, 800°F
B. 600°F, 900°F
C. 800°F, 1000°F
D. 700°F, 1100°F: B
281. Nitriding is usually confined to the surface of most
components and will have a dull, ________ appearance. In
more advanced stages, the material will exhibit very hard
surface hardness.
A. Gray
B. Black
C. Brown
D. White: A
282. Nitriding layers are magnetic. Therefore, _________ should be
checked for magnetism as an initial screening for nitriding.
A. 300 Series SS
B. 400 Series SS
C. Duplex SS
D. Low alloy steel.: A
283. Non-stressed relieved _________ is susceptible to stress
corrosion cracking when in contact with moist HF vapors in
the presence of oxygen.
A. Carbon steel
B. Alloy 400
C. 300 Series SS
D. 400 Series SS: B
284. __________ of a component is the most important factor in
determining a components resistance to mechanical
fatigue.
A. Design
B. Temperature
C. Stress
D. Pressure: A
285. __________ of the amine system is the most effective way to
prevent amine corrosion.
A. Proper concentration
B. Proper operation
C. Proper design
D. Proper startup: B
286. Once cracking from LME has occurred, grinding out the
affected area ______ an acceptable fix.
A. Is
B. Is not
C. Can be
D. Cannot be: B
287. Oxidation of carbon steel begins to become significant
above ________.
A. 800°F
B. 900°F
C. 1000°F
D. 1100°F: C
288. Oxygen and iron in the water injected into reactor effluent
can lead to __________ corrosion and fouling.
A. Increased
B. Decreased
C. Substantial
D. Minimal: A
289. Permanent deformation occurring at relatively low stress
levels as a result of localized overheating is called _______.
A. Stress cracking
B. Brittle fracture
C. Temper embrittlement
D. Stress rupture: D
290. Phosphoric acid corrosion is usually found in ________ areas.
A. High velocity
B. Low Velocity
C. High temperature
D. Low temperature: B
291. The presence of _________ can destabilize the scale and turn
it into a non protective scale.
A. H²S
B. O²
C. H²
D. H²O: D
22 / 37
24. 292. The presence of _______ in H²S streams increases the
severity of high temperature sulfide corrosion at
temperature above about 500°F
A. Amine
B. Hydrogen
C. Sulfides
D. All of the above: B
293. The presence of what other element increases the
propensity for CI SCC cracking?
a. Carbon dioxide.
b. Oxygen.
c. Carbon monoxide.
d. Nitrogen.: B
294. Preventative measures to minimize the potential for brittle
fracture in existing equipment are limited to controlling
________ and _________, minimizing pressure at ambient
temperatures during start-up and shutdown and periodic
inspections at high stress locations.
A. Temperature, stress
B. Stress, pressure
C. Velocity, stress
D. Temperature, pressure: D
295. Primarily hot-wall piping and equipment in the following
units can be affected by graphitization. FCC, catalytic
reformer and ________.
A. Hydrotreater
B. Hydrocracker
C. Coker
D. Alky: C
296. The primary factors affecting high temperature oxidation
are metal temperature and ______.
A. Pressure
B. Alloy composition
C. Stress
D. Oxygen: B
297. A prime location for erosion is:
A. In catalyst piping
B. Downstream of a gate valve
C. Any superheated steam piping
D. Upstream of a pump: A
298. Proper application of ________ will control but not eliminate
microbes that cause MIC so that continued treatment is
necessary.
A. Ozone
B. Caustic
C. Biocides
D. None of the above: C
299. Protection in a boiler from boiler feed water corrosion is
accomplished by:
A. Injecting chlorines to kill microbiological bugs
B. Injecting caustic to lower the pH to <4.0
C. Lowering solids content in boiler feed water to less than
50 ppm.
D. Maintaining a protective corrosion layer of magnetite
(Fe304): D
300. PWHT is _____________ in preventing caustic SCC.
A. Effective
B. Not effective
C. Not practical
D. None of the above: A
301. A quick test for embrittlement from _________ is a bend test
or crush test. Unaffected material will be crushed in a
ductile fashion while embrittled components will crack with
no signs of ductility.
A. Titanium Hydriding
B. Temper embrittlement
C. Caustic embrittlement
D. None of the above: A
302. The rate of creep deformation is a function of the material,
load and temperature. The rate of damage is sensitive to
both load and temperature. Generally, an increase of about
_____ or an increase of _________ on stress can cut the
remaining life in half.
A. 25°F, 15%
B. 50°F, 10%
C. 50°F, 15%
D. 25°F, 10%: A
303. Refractory anchor material must be compatible with the
_________ of the base metal.
A. Composition
B. Welding
C. Thermal coefficient
D. Ductility: C
304. Refractory anchors must be resistant to _________ in high
temperature services.
A. Thermal fatigue
B. Thermal cracking
C. Stress cracking
D. Oxidation: D
305. Refractory lined equipment should be designed for
erosion, thermal shock and ________.
A. Thermal fatigue
B. Thermal expansion
C. Thermal contraction
D. All of the above: B
23 / 37
25. 306. The regenerator reboiler and the regenerator are areas
where the temperature and ________ of the amine stream are
the highest and can cause significant corrosion problems.
A. Pressure
B. Stress
C. Turbulence
D. Concentration: C
307. Regular and controlled carbon grades of stainless steels
such as types 304/304H and 316/316H are particularly
susceptible to sensitization in the weld HAZ. Low carbon "L"
grades are less susceptible and usually can be welded
without sensitizing. The "L" grades will not sensitize
provided long term operating temperatures do not exceed
about ________.
A. 700°F
B. 750°F
C. 800°F
D. 900°F: B
308. Reheat cracking is most frequently observed in __________
grained sections of a heat-affected zone.
A. Course
B. Fine
C. Dense
D. Treated: A
309. The removal of a materials protective scale by impacting
materials is called:
A. Erosion
B. Erosion-corrosion
C. Erosion or erosion-corrosion
D. IPRSC (imparting particle removal of scale corrosion): B
310. The removal of surface material by impacting materials is
called:
A. Erosion
B. Erosion-corrosion
C. Erosion or erosion-corrosion
D. IPC (imparting particle corrosion): A
311. Resistance to sulfidation increases as the :
A. Chromium content in the material increases
B. Nickel content in the material increases
C. Material's tensile strength decreases
D. Material's tensile strength increases: A
312. SCC tendency __________ towards the alkaline pH region.
A. Decreases
B. Increases
C. Remains constant
D. Varies: A
313. SCC usually occurs at pH values above two(2). SCC
tendency __________ toward the alkaline pH region.
A. Increases
B. Decreases
C. Stabilizes
D. None of the above: B
314. Sensitization occurs in the _________ to ________ range.
A. 800°F, 1400°F
B. 750°F, 1500°F
C. 600°F, 1120°F
D. 1000°F, 1750°F: B
315. The severity of hydrochloric acid corrosion _______ with _______
HCI concentration and increasing temperatures.
A. Decreases, decreasing
B. Increases, increasing
C. Decreases, increasing
D. Increases, decreasing: B
316. Short term overheating is a permanent deformation
occurring at relatively ________ stress levels as a result of
localized overheating. This usually Results in bulging and
failure by stress rupture.
A. Low
B. High
C. Even
D. None of the above: A
317. Sigma phase in welds can be minimized by controlling
ferrite in the range of ___________ for Type 347 SS
A. 3%-5%
B. 5%-7%
C. 7%-9%
D. 5%-9%: D
318. Sigma phase occurs in Ferritic, martensitic, austenitic and
duplex stainless steel when exposed to temperatures in the
range of _________.
A. 538°C - 927°C
B. 614°C - 918°C
C. 676°C - 760°C
D. 584°C - 840°C: A
319. Sigma phase occurs in Ferritic, martensitic, austenitic and
duplex stainless steel when exposed to temperatures in the
range of _________.
A. 850F - 1250F
B. 1000F - 1700F
C. 950F - 1500F
D. 800F - 1500F: B
24 / 37
26. 320. The signature mark of a fatigue is a _______ type fingerprint
that has concentric rings.
A. Eyebrow
B. Half-moon
C. Radii
D. Clam Shell: D
321. ___________ significantly increases the probability and severity
of blistering, HIC and SOHIC.
A. Hydrogen
B. Oxygen
C. Cyanide
D. Caustic: C
322. __________ significantly increases the probability and severity
of blistering, HIC SOHIC damage.
A. Caustic
B. Cyanides
C. Stress
D. Temperature: B
323. Since all fuels contain some amount of sulfur, sulfuric and
sulfurous acid __________ can occur if the metal temperature is
below this temperature.
A. Corrosion
B. Pitting
C. Dew point corrosion
D. All of the above: C
324. Since cracking is usually surface connected, effective
methods of inspection are:
a. WFMT and LT.
b. ET. and AE.
c. VT. MT and PT.
d. AET, ET. and RT.: C
325. Smooth grooving of pipe walls is an indication that is the
causative agent.
a. carbon monoxide
b. oxygen
c. carbon dioxide
d. hydrochloric or sulfuric acids: C
326. SOHIC is driven by localized stresses so that ___________ is
somewhat effective in preventing SOHIC damage.
A. PWHT
B. Preheat
C. Temperature
D. None of the above: A
327. Soil corrosion appears as external thinning with localized
losses due to _______.
A. Resistivity
B. Pitting
C. General corrosion
D. Potential: B
328. Soil corrosion of carbon steel can be minimized through
the use of special backfill, coating and _________.
A. Cathodic protection
B. Resistivity
C. Temperature
D. None of the above: A
329. Soils having high moisture, high dissolved salt concentration
and high ____________ are the most corrosive.
A. Oxygen content
B. Resistivity
C. Acidity
D. All of the above: C
330. Soil to Air interface areas are usually more susceptible to
corrosion than the rest of the structure because of _________
and ___________ availability.
A. Moisture
B. Bacteria
C. Oxygen
D. B and C
E. A and C: E
331. Some units affected by HTHA are listed below. One of the
ones listed is usually not considered a target. Pick this unit.
a. Hydrocracker.
b. Crude still.
c. Catalytic Reformer.
d. Hydrotreater.: B
332. Sour water corrosion in ___________ containing environments
may be accompanied by carbonate SCC.
A. H²O
B. H²S
C. CO²
D. O²: C
333. Spheroidization and graphitization are competing
mechanism that occur at overlapping temperature ranges.
Spheroidization tends to occur above _______ while
graphitization predominates below this temperature.
A. 1000°F
B. 1025°F
C. 1050°F
D. 1100°F: B
25 / 37
27. 334. SSC generally occurs below about _______.
A. 150°F
B. 180°F
C. 210°F
D. 240°F: B
335. SSC generally occurs below about _________.
A. 225°F
B. 200°F
C. 180°F
D. 150°F: C
336. SSC is a form of hydrogen stress cracking resulting from
the absorption of atomic hydrogen that is produced by the
________ corrosion process in the metal surface.
A. HCl
B. HF
C. Sulfide
D. Wet H²S: C
337. SSC is a form of hydrogen stress cracking resulting from
the absorption of _________ that is produced by the sulfide
corrosion process on the metal surface.
A. Sulfur dioxide
B. Hydrogen sulfide
C. Atomic hydrogen
D. Hydrogen chloride: C
338. SSC is a form of _________ stress corrosion cracking.
A. Hydrogen
B. Caustic
C. Polythionic
D. Alkaline: A
339. Stainless steel cyclones, piping ductwork and valves in high
temperature FCC regeneration service are susceptible
areas for ____________.
A. Brittle fracture
B. Sigma phase
C. Cavitation
D. Corrosion fatigue: B
340. Stainless steels have higher coefficients of thermal
expansion than carbon steel or low alloy steel or nickel
based alloys and are more likely to see ________.
A. Higher temperatures
B. Higher stresses
C. Higher pressure
D. None of the above: B
341. Stainless steels with sigma can normally withstand normal
operating stresses but upon cooling to temperatures below
______ may show a complete lack of fracture toughness as
measured by a Charpy impact test.
A. 800°F
B. 600°F
C. 500°F
D. 400°F: C
342. Start-up and shutdown of equipment increase the
susceptibility of thermal fatigue. There is no limit on
temperature swings; however, as a practical rule, cracking
may be suspected if the temperature swing exceeds about
_______.
A. 150°F
B. 200°F
C. 250°F
D. 300°F: B
343. A Steam actuated soot blower has condensate in the first
steam exiting the soot blower. What type of damage can be
expected to be found when the furnace is brought down for
maintenance and inspection?
A. Thermal fatigue
B. Steam blanketing
C. Creep
D. Stress rupture: A
344. Steam blanketing is when the heat flow balance is
disturbed; individual bubbles join to form a steam blanket, a
condition known as Departure from Nucleate Boiling (DNB).
Once a steam blanket forms, tube rupture can occur
rapidly, as a result of __________.
A. Thermal fatigue
B. Short term overheating
C. Brittle fracture
D. Stress: B
345. Steel cleanliness and ________ have a significant influence on
toughness and resistance to brittle fracture.
A. Composition
B. Alloy
C. Grain Size
D. None of the above: C
346. Steel hardness, ________ and stress are critical factors in
causing hydrogen stress cracking.
A. Temperature
B. Alloy composition
C. Strength
D. None of the above: C
26 / 37
28. 347. Stress corrosion cracking usually occurs at metal
temperatures above about:
a. 200 F.
b. 160 F.
c. 140 F.
d. 100 F.: C
348. Stresses acting on the weldment are significantly __________
when austenitic stainless steel filler metal is used. A nickel
based filler has a coefficient of thermal expansion closer to
carbon steel resulting in a significantly lower stress at
elevated temperatures.
A. Lower
B. Higher
C. Altered
D. None of the above: B
349. Stress levels and ________ are the critical factors causing
carbonate stress corrosion cracking.
A. Temperature
B. Velocity
C. Water chemistry
D. None of the above: C
350. Stress relief and stabilization heat treatment of 300 Series
SS for maximizing chloride SCC and PASCC resistance can
cause __________ problems, especially in thicker sections.
A. Thermal fatigue
B. Reheat cracking
C. Hydrogen
D. HIC: B
351. Stress ruptures are characterized by _________ failures and
are usually accompanied by thinning at the fracture surface.
A. Rapid
B. Fish-mouth
C. Tensile
D. None of the above: B
352. The sudden rapid fracture under stress (residual or applied)
where the material exhibits little or no evidence of ductility
or plastic deformation is called __________.
A. 885°F
B. Temper embrittlement
C. Stress corrosion cracking
D. Brittle fracture: D
353. Sufidation is also known as ________.
A. Sulfur corrosion
B. Sulfate corrosion
C. Sulfidic corrosion
D. None of the above: C
354. Sulfidation is primarily caused by _________ and other
reactive sulfur species as a result of the thermal
decomposition of sulfur compounds at high temperatures.
A. Sulfur dioxide
B. H²S
C. Sulfur trioxide
D. Sulfates: B
355. Sulfidation is primary caused by:
A. Impacting particles
B. Sulfur compounds decomposing at higher temperatures
C. Sulfur compounds being created in the FCCU (cat
cracking unit)
D. Elemental sulfur collecting in stagnate areas, e.g. dead
legs.
E. Operators failing to adequately control the pH of sulfur
streams.: B
356. Sulfidation of iron-based alloys usually begins at about:
A. 150°F
B. 250°F
C. 500°F
D. 1100°F: C
357. Sulfidation of iron-based alloys usually begins at metal
temperature above __________.
A. 500°F
B. 600°F
C. 800°F
D. 1000°F: A
358. Sulfidation of iron-based alloys usually begins at metal
temperatures above
a. 800°F
b. 700°F
c. 600°F
d. 500°F: D
359. Sulfidation usually creates:
A. Uniform corrosion
B. Isolated pitting
C. Intergranular cracking
D. Transgranular cracking
E. Hard and brittle zones
F. Inspection mightmares: A
360. Sulfide stress cracking (SSC) is defined as cracking of metal
under the combined action of tensile stress and corrosion
in the presence of ___________ and ___________.
A. Sulfur, Oxide
B. Hydrogen, water
C. H²S, Oxygen
D. Water, H²S: D
27 / 37
29. 361. Sulfur and chloride species in fuel will form sulfur dioxide,
sulfur trioxide and hydrogen chloride within the combustion
products. At low enough temperatures, these gases and the
water Vapor in the flue gas will condense to form ___________
acid.
A. Hydrochloric
B. Hyrdofluoric
C. Sulfuric
D. Both A and C: D
362. Sulfur compounds react with carbon steel in high
temperature environments. This reaction causes corrosion.
The presence of____________ accelerates the corrosion.
a. water
b. carbon dioxide
c. oxygen
d. hydrogen: D
363. Sulfuric acid promotes general and localized corrosion of
carbon steel. Carbon steel heat affected zones may
experience severe corrosion. Acid concentration,
temperature, alloy content and _______ are critical factors
affecting sulfuric acid corrosion.
A. Pressure
B. Stress
C. Velocity
D. Ductility: C
364. Surface initiated cracks caused by environmental cracking
of 300 Series SS and some nickel based alloys under
combined action of tensile stress, temperature and aqueous
chloride environmental is called _________. The presence of
dissolved oxygen _________ the propensity for cracking.
A. CI SCC, increases
B. Stress cracking, increases
C. CI SCC, Decreases
D. Stress cracking, Decreases: A
365. Susceptibility of an alloy to sulfidation is determined by its
ability to form protective _____________.
A. Oxide scales
B. Sulfide scales
C. Carbide scales
D. None of the above: B
366. Susceptibility to hydrogen stress cracking __________ with
_________ hardness.
A. Increases, increasing
B. Decreases, increasing
C. Decreases, Decreasing
D. Both A and C: D
367. Susceptibility to sulfidation is determined by the _______ of
the material.
A. Corrosion resistance
B. Tensile strength
C. Chemical composition
D. Yield Strength: C
368. Susceptibility to temper embrittlement is largely
determined by the presence of the alloying elements
manganese and _______.
A. Chromium
B. Moly
C. Silicon
D. None of the above: C
369. Temperature, ___________ and stress are critical factors of
stress rupture. This is usually found in furnaces with cooking
tendencies and fired heater tubes.
A. Pressure
B. Ductility
C. Time
D. Tensile strength: C
370. Temper embrittlement ____________ be prevented if the
material contains critical levels of embrittling impurity
elements and is exposed in the embrittlement range.
A. Can
B. Cannot
C. Will
D. None of the above: B
371. Temper embrittlement can be identified by a(n) ________ shift
in the ductile-to-brittle transition temperature measured in
a Charpy impact test.
A. Upward
B. Downward
C. Abrupt
D. None of the above: A
372. Temper embrittlement is a metallurgical change that is not
readily apparent and can be confirmed through _________.
A. Metallographic examination
B. Impact testing
C. Metallography
D. None of the above: B
373. __________ testing is the best method to determine the
susceptibility of a material to hydrogen stress cracking.
A. Hardness
B. Acoustic
C. SWUT
D. AUT: A
28 / 37
30. 374. There is currently no known metal alloy that is immune to
_________ under all conditions.
A. Carburization
B. Metal dusting
C. Decarburization
D. None of the above: B
375. Thermal fatigue becomes of concern if the temperature
swings exceed:
A. 50°F
B. 100°F
C. 200°F
D. 400°F: C
376. Thermal fatigue cracks propagate ____________ to the stress
and are usually dagger shaped, transgranular and oxide-
filled.
A. Axial
B. Diagonal
C. Transverse
D. Angular: C
377. Thermal fatigue cracks usually:
A. initiate on the surface of the component
B. Initiate in the subsurface of the component
C. Grow very rapidly (at the speed of sound in the material)
D. Are very tight and narrow: A
378. Thermal fatigue cracks usually initiate on the _______ of the
component. They are generally wide and filled with oxides
due to the elevated temperatures.
A. Surface
B. ID
C. Welds
D. None of the above: A
379. Thermal fatigue cracks usually propagate ________ to the
stress and they are usually dagger-shaped.
A. Parallel
B. Diagonal
C. Transverse
D. Across: C
380. Thermal fatigue damage is in the form of cracking that may
occur anywhere in a metallic component where relative
movement is constrained, particularly under repeated
________.
A. Cyclic stresses
B. Thermal cycling
C. Pressure variations
D. All of the above: B
381. Thermal fatigue is caused by:
A. Cyclic stresses that come from temperature variations
B. Long term operation at elevated temperatures
C. Excessive thermal growth
D. Hours of physical activity during a hot summer day: A
382. Three factors when critically combined tend to cause
brittle fracture. Which of the four factors
listed below does not belong?
a. The material's fracture toughness (resistant to crack like
flaws) is low.
b. The size, shape and stress concentration of a flaw tends
to lead to failure.
c. The temperature is high enough to induce failure.
d. The amount of residual and applied stresses on the flaw
is enough to cause fracture.: C
383. Three of the steels listed below are susceptible to brittle
fracture. Pick the one that is not.
a. Carbon steel.
b. 300 series of stainless steels.
c. Low alloy steel.
d. 400 series of stainless steels: B
384. Three types of equipment with mechanical loading that are
affected by mechanical fatigue cracking are listed below.
One of the four items listed below is not correct. Pick the
incorrect item.
a. Rotating shafts on centrifugal pumps that have stress
concentrations due to key ways.
b. Small diameter piping that vibrates because of adjacent
equipment.
c. Large, heavy, cast steel compressor cases.
d. High pressure drop control valves or steam reducing
stations that have serious vibration problems: C
385. Time to failure by thermal fatigue is primarily affected by:
A. Magnitude of stress and operating temperature
B. Magnitude of stress and number of cycles
C. Carbon content in material and operating temperature
D. Carbon content in material and number of cycles.: B
386. Titanium Hydriding damage occurs primarily in sour water
strippers and amine units in the overhead condensers, heat
exchanger tubes and other titanium equipment operating
above ________.
A. 300°F
B. 270°F
C. 210°F
D. 165°F: D
29 / 37
31. 387. Titanium should not be used in known hydriding services
such as ______ or _____.
A. Caustic, amine
B. Amine, sour water
C. Sour water, Alkylation
D. All of the above: B
388. To prevent carburization, select alloys with strong surface
oxide or sulfide film former such as _________.
A. Silicon
B. Molybdenum
C. Aluminum
D. Both A and C: D
389. To prevent hydrogen embrittlement, use lower strength
steels and __________ to temper the microstructure, improve
ductility and reduce residual stress.
A. Alloys
B. Preheat
C. PWHT
D. All of the above: C
390. Type 304L SS is satisfactory for phosphoric acid
concentration of 100% up to about ___________. Type 316L is
required from there to 225°F.
A. 140°F
B. 150°F
C. 100°F
D. 120°F: D
391. Typical HF Alkylation units operate with 1% to 3% water in
the acid, equivalent to an HF-in-water concentration of
97% to 99% and the temperatures are generally below
__________.
A. 300°F
B. 250°F
C. 200°F
D. 150°F: D
392. Units where graphitization may be suspected are the FCCU
and the _______ unit.
A. Hydrotreater
B. Coker
C. Alky
D. None of the above: B
393. __________ usually occurs when a colder liquid contact a
warmer metal surface.
A. Brittle fracture
B. Thermal fatigue
C. Thermal shock
D. Stress rupture: C
394. __________ usually occurs when a colder liquid contact a
warmer metal surface.
A. Stress cracking
B. Thermal fatigue
C. Thermal shock
D. Stress shock: C
395. A vacuum tower operating at 740°F is being entered to
inspect. Several sets of Type 410 SS trays are bent at
various angles. The trays are removed in order to straighten
them. When an attempt is made to straighten them cracks
form at the bends. What type of damage mechanism would
cause the cracks to form?
A. Hydrogen embrittlement
B. Sulfide stress corrosion cracking
C. 885°F embrittlement
D. High temperature corrosion: C
396. Vessels constructed after December, 1987 are subject to
the requirements of _________ of ASME Section VIII, Division
1.
A. UW-26
B. UG-31
C. UB-54
D. UCS-66: D
397. Vibration-induced fatigue can be eliminated or reduced
through _________ and the use of supports and vibration
dampening equipment. Material upgrades are not usually a
solution.
A. Hangers
B. Dummy legs
C. Design
D. None of the above: C
398. Ways to prevent thermal fatigue include stress
concentrators by making _________________ transitions at places
where the wall thickness changes.: smooth
399. Weld heat affected zone graphitization is most frequently
found in the heat affected zone adjacent to welds in
narrow band, corresponding to the low temperature edge
of the heat affected zone, in multi-pass welded butt joints,
these zones overlap each other covering the entire cross
section. Because of its appearance, this type of
graphitization is called ____________.
A. Half-moon
B. Eyebrow
C. Radii
D. None of the above: B
30 / 37
32. 400. Welds joining dissimilar materials (ferritic and austenetic)
may suffer ___________ related damage at high temperature
due to thermal expansion stresses.
A. Stress
B. Creep
C. Fatigue
D. Thermal stress: B
401. Wet H²S services or ___________ acid services are process
where hydrogen diffuses into the steel and hydrogen
embrittlement (HE) is an issue.
A. HF
B. Sulfuric
C. Caustic
D. HCL: A
402. What alloying element determines the resistance of an
alloy to sulfidation?
a. Nickel.
b. Chrome.
c. Low carbon.
d. Columbium.: B
403. What determines the likelihood and severity of corrosion
for flue gas dew point corrosion?
a. concentration of sulfur and chlorides in the fuel.
b. an excess of vanadium in the fuel.
c. condensation of hydrofluoric acid.
d. none of the above.: A
404. What determines the susceptibility of an alloy to
sulfidation?
a. Its ability to form protective sulfide scales.
b. The amount of nickel present.
c. The ability to resist erosion.
d. The capability to avoid graphitic decomposition.: A
405. What is not a proven method for the detection of HTHA
damage?
a. VT.
b. AET.
c. WFMT.
d. RT: B
406. What is the atmospheric corrosionrate if carbon steel is
exposed in a dry rural environment?
a. <4 mpy
b. <3 mpy
c. <2 mpy
d. <1 mpy: D
407. What is the chemical symbol for butane of butylenes?
A. C²
B. C3
C. C4
D. CH4: C
408. What is the chemical symbol for ethane or ethylene?
A. C²
B. C3
C. C4
D. CH4: A
409. What is the chemical symbol for propane or propylene?
A. C²
B. C3
C. C4
D. CH4: B
410. What is the typical erosion-corrosion rate in mpy of Monel
immersed in a seawater flume with the seawater traveling
over it at 4 fps?
a. 0.2 mpy
b. <0.2mpy
c. 1 mpy
d. 0.3 mpy: B
411. What kind of steel is not susceptible to SCC?
a. AISI Type 347 SS.
b. AISI Type 316 SS.
c. Carbon steel.
d. Duplex SS: C
412. What materials are affected most by atmospheric
corrosion?
a. Nickel200, Inconel, and Incoloy.
b. Monel, Titanium, Duranickelalloy 301.
c. 300series stainless steels, and cast iron.
d. Carbon steel, low alloy steels, and copper alloyed
aluminum.: D
413. What materials are usually affected by CUI?
a. Cast iron, Nickel 2OO, and Aluminum.
b. Titanium, Duranickel alloy 301, and Copper nickel.
c. Monel, incoloy, and inconel.
d. Carbon steel, low alloy steels, 300 series and duplex
stainless steels.: D
414. What method is most used to assure boiler feed water
corrosion is not occurring?
A. Spot UT readings at turbulent areas
B. Profile RT at turbulent areas
C. Profile RT and stagnant
D. Laboratory analysis of boiler feedwater: D
415. What percent of chlorides is safe for exposure to 300 series
stainless steel?
a.15%
b.10%
c.5%
d.O%: D
31 / 37
33. 416. What standard refers to Fitness-For-Service evaluations?
A. RP 581
B. RP 579
C. RP 588
D.RP 568: B
417. What standard refers to Risk-Based-Inspection?
A. RP 581
B. RP 579
C. RP 588
D. RP 568: A
418. What structure is 304 stainless steel?
A. Martensitic
B. Austenitic
C. Duplex
D. Ferritic: B
419. What structure is 409 stainless steel?
A. Martensitic
B. Austenitic
C. Duplex
D. Ferritic: D
420. What structure is 410 stainless steel?
A. Martensitic
B. Austenitic
C. Duplex
D. Ferritic: A
421. What test is used to determine a materials's toughness?
A. Charpy impact test
B. Guided Bend test
C. Tension Test
D. Physical fitness test: A
422. What treatment is used to prevent boiler feed water
corrosion?
A. Oxide scavengers are added to process
B. Oxygen scavengers are added to process
C. Sulfide scavengers are added to process
D. Sulfur scavengers are added to process: B
423. What type damage is caused by thermal fatigue?
a. Damage is in the form of severe oxidation and scaling.
b. Damage is in the form of cracking anywhere a movement
or expansion is constrained.
c. Damage is in the form of tensile separation of high
stressed parts of equipment.
d. Damage is in the form of bending of parts that are highly
stressed.: B
424. What type of on stream inspection method can detect the
loss of refractory on an operating unit?
a. Visual inspection.
b. Infrared scan.
c. Ultrasonic scan.
d. Eddy current scan.: B
425. What type of unit suffers severe erosion-corrosion due to
exposure to naphthenic acids in
some crude oil?
a. Catalytic Reformer Reactor piping.
b. FCCU Fractionator overhead lines.
c. Hydroprocessing reactor effluent piping.
d. Crude and Vacuum unit piping and vessels.: D
426. What usually causes corrosion in boiler feedwater and
condensate return systems?
a. Corrosion pitting is the result of dezincification of the
tubes.
b. Corrosion is the result of dissolved heavy water (020) and
carbon monoxide (CO).
c. Corrosion is the result of HCI and H2SO4in the system.
d. Corrosion is the result of dissolved gases, oxygen and
carbon dioxide.: D
427. When carbon is absorbed into a material at elevated
temperatures while in contact with a carbonaceous
substance it is called carburization. Temperatures usually
have to be above __________ for this to occur.
A. 1000°F
B. 1100°F
C. 1200°F
D. 1400°F: B
428. When caustic stress corrosion cracking is a concern, steam
out of ___________ carbon steel piping and equipment should
be avoided.
A. PWHT
B. Non-PWHT
C. Ferritic
D. Hardened: B
429. When connected to a more anodic material, titanium may
suffer severe __________.
A. Corrosion
B. Hydriding
C. Stress
D. Notch toughness: B
430. Where is PASCC normally located?
A. Adjacent to welds
B. On impellers
C. At stress risers
D. At flanges: A
32 / 37
34. 431. Which API RP recommends programs to monitor small-bore
piping, flange faces, blistering and HIC/SOHIC if HF alky
units?
A. 574
B. 751
C. 571
D. 980: B
432. Which if the following materials are subject to mechanical
fatigue?
A. Carbon steels
B. Stainless steels
C. Low alloy steels
D. All of the above: D
433. Which material below is not susceptible to caustic
corrosion?
A. Carbon steel
B. 400 Series SS
C. 300 Series SS
D. Low alloy steel: B
434. Which material does not have endurance limit?
A. Non-normalized carbon steel
B. Normalized carbon steel
C. Stainless Steel
D. Titanium: C
435. Which of following materials are not susceptible to
hydrogen stress cracking?
A. Carbon steel
B. Low alloy steel
C. Stainless steel
D. None of the above: C
436. Which of the following alkanolamine systems is the least
aggressive in causing amine corrosion?
A. Monoethanolamine (MEA)
B. Diglycolamine (DGA)
C. Diethanolamine (DEA)
D. Methyldiethanolamine (MDEA): D
437. Which of the following alkanolamine systems is the most
aggressive in causing amine corrosion?
A. Monoethanolamine (MEA)
B. Diglycolamine (DGA)
C. Diethanolamine (DEA)
D. Methydiethanolamine (MDEA): A
438. Which of the following are affected by sulfidation?
A. Carbon steel
B. 300 Series SS
C. 400 Series SS
D. All of the above: D
439. Which of the following are susceptible to thermal fatigue?
A. SA-516-70
B. SA-182 Gr B
C. SA-53 Gr B
D. All of the above: D
440. Which of the following can be affected by 885°F
Embrittlement?
A. 410 SS
B. 430 SS
C. 308 SS
D. Alloy 2205
E. A,B and D: E
441. Which of the following does not increase the likelihood of
atmospheric corrosion?
A. Bird poop
B. Increasing annual rainfalls
C. Locations where moisture
D. Increasing operating pressures
E. Increasing amounts of airborne contaminates: D
442. Which of the following is not a critical factor that
contributes to a brittle fracture?
A. The material's fracture toughness
B. Maximum operating temperature
C. Stress concentration at at flaw
D. Magnitude of the residual stresses: B
443. Which of the following is not a major factor associated with
boiler water condensate corrosion?
A. Operating pressure
B. Oxygen
C. Carbon dioxide content
D. Process pH
E. Temperature: A
444. Which of the following is not a major factor associated with
corrosion by sulfidation?
A. Alloy composition
B. Operating pressure
C. Operating temperature
D. Sulfur content: B
445. Which of the following is not a method used to prevent
brittle fracture?
A. Thorough inspections
B. Strict controls on selecting construction materials
C. Post weld heat treatment
D. Controlling minimum operating temperatures: A
33 / 37
35. 446. Which of the following is not a primary factor contributing
to erosion-corrosion?
A. Impact angle (angle that impacting particles strike metal)
B. Tensile strength of the metal
C. Velocity of impacting particles
D. Corrosiveness of the environment.: B
447. Which of the following is not a prime candidate for thermal
fatigue?
A. Coke drums
B. Steam actuated soot blowers
C. Mix points of hot and cold streams
D. 600 psig steam piping
E. Welds joining materials having different coefficients of
expansion: D
448. Which of the following is not primary factor contributing to
erosion?
A. Impact angle (angle that impacting particles strike metal)
B. Size if impacting particles
C. Velocity of impacting particles
D. Density of impacting particles
E. Corrosiveness of the environment.: E
449. Which of the following is not primary initiating point for
thermal fatigue?
A. Notches
B. Rounded pits
C. Nozzle-to-shell welds
D. Weld toes: B
450. Which of the following materials are affected by
mechanical fatigue cracking?
A. Only carbon steel
B. Only carbon steel and chromes
C. Only carbon steel and high nickel alloys
D. All materials: B
451. Which of the following materials are generally not suitable
for HF service?
A. 300 Series SS
B. Carbon Steel
C. 400 Series SS
D. Both A and C: D
452. Which of the following materials are susceptible to
nitriding?
A. Carbon Steel
B. 300 Series SS
C. 400 Series SS
D. All of the above: D
453. Which of the following materials are susceptible to
polythionic acid SCC?
A. 300 Series SS
B. Alloy 600
C. Alloy 800
D. All of the above: D
454. Which of the following materials are the least susceptible
to caustic embrittlement?
A. Carbon steel
B. Stainless steel
C. 9Cr-0.5Mo
D. Nickel base alloys: D
455. Which of the following materials is affected by high
temperature corrosion?
A. Carbon Steel
B. 300 Series SS
C. 400 Series SS
D. All of the above: D
456. Which of the following materials is least affected by
atmospheric corrosion?
A. Carbon steel
B. Chromes
C. Stainless steels
D. Copper alloyed with alumimum: C
457. Which of the following materials is least effected by brittle
fracture?
A. Carbon Steel
B. Chromes
C. 300 Series stainless steels
D. 400 Series stainless steel
E. All Stainless steels: C
458. Which of the following materials is not susceptible to CI
SCC?
A. 400 Series SS
B. Duplex SS
C. Nickel based alloys
D. All of the above: A
459. Which of the following materials is not susceptible to high
temperature hydrogen attack?
A. 300 Series SS
B. 5Cr-1Mo
C. 9Cr-1Mo
D. All of the above: D
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36. 460. Which of the following materials is not susceptible to SCC?
A. Carbon steel
B. 300 Series SS
C. Low alloy steel
D. Both A and C: D
461. Which of the following materials is susceptible to
carburization?
A. Low alloy steels
B. 300 Series SS
C. 400 Series SS
D. All of the above: D
462. Which of the following materials is susceptible to CO²
corrosion?
A. Carbon steel
B. Stainless steel
C. Duplex stainless steel
D. Both B and C: A
463. Which of the following materials is susceptible to sigma
phase embrittlement?
A. Carbon Steel
B. Low alloy
C. 300 Series SS
D. Both A and B: C
464. Which of the following metals is the most anodic?
A. Zinc
B. Carbon Steel
C. Nickel
D. Monel: A
465. Which of the methods are effective for finding thermal
fatigue cracks?
A. MT
B. PT
C. VT
D. All of the above: D
466. Which of these cast irons are not susceptible to graphitic
corrosion?
A. Gray cast iron
B. Black cast iron
C. White cast iron
D. None of the above: C
467. Which of these materials are not susceptible to PASCC?
A. Carbon steel
B. 300 Series SS
C. 400 Series SS
D. Both A and C: D
468. Which of these materials are not susceptible to
Spheroidization?
A. Carbon Steel
B. 9Cr-1Mo
C. 316 SS
D. Both A and B: C
469. Which of these materials are susceptible to brittle fracture?
A. Carbon steels
B. Low alloy steels
C. 400 Series SS
D. All of the above: D
470. Which of these materials are susceptible to creep damage?
A. Carbon Steel
B. Stainless Steel
C. Low alloy steel
D. All of the above: D
471. Which of these materials exhibit an endurance limit below
which fatigue cracking will not occur?
A. Carbon Steel
B. 300 Series SS
C. 400 Series SS
D. None of the above: A
472. Which of these materials is not susceptible to amine
cracking?
A. Carbon steel
B. 300 Series SS
C. 400 Series SS
D. Both B and C: D
473. Which of these materials is susceptible to 885°F
embrittlement?
A. 400 Series SS
B. Duplex SS
C. 5Cr-1Mo
D. Both A and B: D
474. With 885°F embrittlement, increasing amounts of _______
increase susceptibility to damage when operating in the
high temperature range of concern.
A. Chromium
B. Hardness
C. Ferrite
D. Hydrogen: C
475. With ammonia stress corrosion cracking weld hardness
should not exceed _______ BHN.
A. 237
B. 225
C. 235
D. 218: B
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37. 476. With chloride stress corrosion cracking, ___________
temperatures ____________ the susceptibility for cracking.
A. Decreasing, Increases
B. Increasing, Increases
C. Increasing, Decreases
D. Decreasing, Eliminates: B
477. With CI SCC, _________ levels of chloride _______ the likelihood
of cracking.
A. Decreasing, Increases
B. Increasing, Decreases
C. Increasing, Increases
D. Increasing, Eliminates: C
478. With CO² corrosion, increasing temperature ________
corrosion rates up to the point where CO² is vaporized.
A. Decrease
B. Increase
C. Eliminate
D. None of the above: B
479. With cooling water corrosion, _________ oxygen content
tends to _______ carbon steel corrosion rates.
A. Increasing, increase
B. Decreasing, decrease
C. Decreasing, increase
D. Increasing, decrease: A
480. With creep, increased stress due to loss in thickness from
corrosion will _________ time to failure.
A. Increase
B. Reduce
C. Not affect
D. None of the above: B
481. With CUI, corrosion rates ________ with increasing metal
temperatures up to the point where the water evaporates
quickly.
A. Decrease
B. Increase
C. Stay the same
D. None of the above: B
482. With decarburization, the decarburized layer will be free of
carbide phases. Carbon steel will be _________.
A. Annealed
B. Quenched
C. Pure Iron
D. None of the above: C
483. With HF acid corrosion, oxygen contamination __________ the
corrosion rate of carbon steel and promotes accelerated
corrosion and SCC of Alloy 400.
A. Increases
B. Decreases
C. Maintains
D. Elimanates: A
484. With high temperature hydrogen attack, ________ using a
combination of velocity ratio and backscatter have been
the most successful in finding cracking.
A. MT
B. UT
C. RT
D. EC: B
485. With high temperature sulfide corrosion (sulfidization),
noticeable increases may be found downstream of ________
injection points.
A. Hydrogen
B. Caustic
C. Ammonia
D. Water: A
486. With hydrofluoric acid corrosion, corrosion rates increase
with ________ temperatures and ________ HF concentrations.
A. Increasing, decreasing
B. Decreasing, increasing
C. Increasing, increasing
D. Decreasing, decreasing: A
487. With short term overheating, time to failure will __________ as
internal pressures or loading decrease.
A. Increase
B. Decrease
C. Remain the same
D. None of the above: A
488. With sour water corrosion, at a given pressure, the H²S
concentration in the sour water _________ as temperatures
__________.
A. Increases, increases
B. Decreases, decreases
C. Increases, decreases
D. Decreases, increases: D
489. With sour water corrosion, corrosion increase with __________
NH4HS concentration and _________ velocity.
A. Increasing, decreasing
B. Increasing, increasing
C. Decreasing, Decreasing
D. Decreasing, increasing: B
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