Piping Material Engineering_November 2024 Batch
Team Piping Engineering
Founder Team Piping Engineering
COMPLETED
Basic course for beginners
Piping Material Engineering_November 2024 Batch
Trainers feedback
4
(51 reviews)
Team Piping Engineering
Founder Team Piping Engineering
Course type
Instructor led live training
Course duration
30 Hrs
Course start date & time
November 16, 2024 at 03:30 PM
Language
English
This course format is where trainer will explain you the subject via online live session. This course will run as per specific date and time.
Why enroll
Comprehensive Understanding: Participants will gain an in-depth knowledge of piping engineering, covering design principles, material specifications, and industry standards comprehensively.
Practical Skills: The course includes hands-on learning with real-world examples and case studies, enabling participants to apply theoretical knowledge to practical scenarios effectively.
Industry-Relevant Insights: Learn about the latest trends, technologies, and best practices in piping engineering, making participants valuable assets to their organizations.
Enhanced Problem-Solving Abilities: Develop advanced skills to diagnose and solve piping design and material specification issues, improving system efficiency and reliability.
Career Advancement: Enhance your professional profile with specialized knowledge and skills in piping engineering, opening up opportunities for career growth in engineering design and project management.
Course details
To equip participants with a comprehensive understanding of piping design, material specifications, and industry standards, enabling them to effectively design, analyze, and manage piping systems in various industrial applications.
This course covers essential aspects of piping engineering, including component identification, valve selection, wall thickness calculations, adherence to codes and standards, material specifications, special parts, and detailed procedures for jacketed piping, piping line lists, and the enquiry process. Gain practical knowledge and skills through a structured syllabus that bridges theoretical concepts with real-world applications.
Course suitable for
Oil & Gas Pharmaceutical & Healthcare Chemical & Process Mechanical Piping & Layout
Key topics covered
Introduction and Piping Components
Overview of piping systems
Identification and functions of piping components
End connections: types and applications
Valves
Types of valves and their applications
Valve selection criteria
Installation and maintenance considerations
Internal Pressure Wall Thickness Calculation
Fundamentals of wall thickness calculation
ASME B31.3 code requirements
Practical examples and calculation techniques
Branch Calculation and External Pressure Wall Thickness Calculation
Branch reinforcement requirements
External pressure considerations
Calculation methods and examples
Codes & Standards and ASME B31.3
Overview of relevant codes and standards
Detailed study of ASME B31.3
Application of codes in piping design
Details of Few Common ASTM Standards
Introduction to ASTM standards
Common ASTM standards used in piping
Material properties and selection criteria
Piping Material Specification & Fluid List in Detail
Understanding piping material specifications (PMS)
Detailed fluid list and compatibility
Material selection for different process conditions
Special Parts
Overview of special piping components
Design and application of special parts
Installation and maintenance considerations
Jacketed Piping with Steam Trap in Detail
Design and application of jacketed piping
Steam trap selection and installation
Thermal insulation and efficiency considerations
Piping Line List and Piping MTO
Creating and maintaining a piping line list
Understanding piping material take-off (MTO)
Importance in project management and cost estimation
Explaining Enquiry and TBA Process
Enquiry process for piping components
Understanding the technical bid analysis (TBA) process
Best practices for ensuring accurate and efficient procurement
Training details
This is a live course that has a scheduled start date.
Live session
November 16, 2024 at 03:30 PM
1 Hours every day
30 Days
Our Alumni Work At
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ITER
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Nirbhay Naik
Engineer
France

LyondellBasell
The learning experience at EveryEng is truly exceptional! The platform is well-organized, making it easy to find relevant courses. The detailed lessons and expert insights are very helpful and helped greatly to improve engineer's technical knowledge.

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The Hague, Netherlands

BBC
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Software Engineer
London

Worley
I’ve had an amazing experience with EveryEng! The courses are well-structured, insightful, and practical. The platform is perfect for anyone looking to advance their engineering career with industry-relevant skills.

Arghyapratim Haldar
Sr Process Engineer
Bangalore, India

SLB
EveryEng stands out with its exceptional learning materials, expert guidance, and real-world applications. It can truly help to enhance skills and knowledge, making more confident professional.

Rajeev Panda
Project Manager
Pune, India
COMPLETED
November 16, 2024
Questions and Answers
A: A feels heavy‑handed, but it's the only step anchored in document control. A line number implies continuity unless a spec break, size break, or class change is explicitly documented. The reducer location alone doesn't justify a silent change. B sounds practical and many projects run that way, but it relies on tribal knowledge rather than traceable approval. C borrows a real erosion argument, yet nothing in the GA proves that intent, and valve sizing logic can't override a missing spec break. D shifts the problem to operations, but the question is about IFC approval, not hydraulic optimization, and you're still left with conflicting controlled documents.
A: A looks slow but it prevents dead‑ends. If the material is wrong, the test is meaningless, and slope issues are easiest to fix before reinstatement. B is tempting under schedule pressure, yet a perfect hydro on the wrong alloy still fails acceptance. C saves scaffold time, but postponing material checks until after access removal is how mismatches survive to startup. D reflects how flushing teams think, but slope is a construction attribute; once fluids are introduced, correction becomes intrusive and risky.
A: A aligns with how the standard is structured: cracking risk ties back to H2S partial pressure and material hardness. B sounds safe, and many specs are written that way, but it's a project overlay, not the base logic of the standard. C mixes two corrosion mechanisms; CO2 affects general corrosion, not SSC susceptibility in the way implied. D feels familiar from some company specs, yet ISO 15156 doesn't set a blanket pressure cutoff for CRA selection.
A: A is the blind spot, literally. A spectacle blind gives positive isolation from upstream flow, which makes B and D feel covered, and it blocks trim leakage paths that worry people during hot work, making C attractive. But once you trap liquid between closed boundaries, the blind does nothing to absorb thermal expansion, and pressure can rise to flange rating fast, especially offshore with sun exposure.
A: A ties together location, morphology, and timing. Low points trap water and solids, setting up localized cells. B explains wall loss but struggles to justify isolated pinholes with good UT elsewhere. C is always tempting when leaks repeat, yet seam defects would track longitudinally, not cluster at low points. D fits elbows and reducers better; straight low points rarely see the shear needed for erosion corrosion.
A: A is the approval stopper because installers need to know what to set in the field. B feels safe, but conservatism doesn't help if the wrong set point is used. C is true in isolation and that's why it distracts, yet it doesn't resolve which condition the drawing intends. D leans on vendor tolerance, but tolerances don't replace clear designation of cold versus operating load.
A: A reflects the failure mechanism standards are guarding against. B sounds process‑savvy, but air ingress actually hurts heat transfer and control. C confuses testing convenience with design intent; vents are controlled features, not auto equalizers. D borrows from inspection language, yet radiography access has nothing to do with jacket venting.
A: A is the hazard path that matters. People often jump to B because it's visible and painful, but it's not the physical risk. C can happen, yet it doesn't tie to the failure of an ESD function. D drifts into control system behavior; plausible in other tests, but not the direct consequence of a valve staying open when it should isolate.
A: A explains both delay and hysteresis with one mechanism. B causes offset and drift, not a sticky response. C affects scaling, yet the physical lag would still be absent. D can cause noise or failure, but it doesn't create a repeatable lag that clears when pressure is held.
A: A ties directly to why graphite‑filled spiral wounds are favored: resilience under cycling. B is a real offshore issue, which makes it tempting, but gasket filler choice doesn't address CUI. C relates to bolting material and lubrication, not gasket construction. D matters during fit‑up, yet spiral wounds aren't selected to forgive poor alignment.
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