UNDERSTANDING PRESSURE VESSEL DESIGN AS PER ASME BPVC CODE

UNDERSTANDING PRESSURE VESSEL DESIGN AS PER ASME BPVC CODE

Shanmugam V

Lead / Senior Mechanical Engineer/Static Equipment Engineer

COMPLETED

7 already enrolled!

Basic course for beginners

Why enroll

Joining an online course on pressure vessel design as per the ASME BPVC code offers numerous advantages for professionals in engineering, manufacturing, and related fields. Here are several compelling reasons to consider:

Comprehensive Understanding of pressure vessel design theories and thereby increasing your knowledge and skills.
Enhanced career opportunities due to high industry demand.
Also, as your understanding over the subject will be more clear, you will be having an edge over your fellow colleagues.
Professional growth.
Flexible Learning Environment.
Practical Sample Problems.
Immediate Doubt clarification.
Certificate of Course Completion.

So, overall an online course on pressure vessel design as per the ASME BPVC code is an invaluable investment for anyone involved in engineering or manufacturing. It not only equips participants with essential knowledge and skills but also enhances their career prospects, ensures compliance with safety regulations, and fosters professional connections. In a field where safety and precision are paramount, such a course can make a significant difference in one’s professional journey.

Opportunities that awaits you!

Earn a course completion certificate

Add this credential to your LinkedIn profile, resume, or CV. Share it on social media and in your performance review

Career opportunities

Sales Executive

EveryEng Engg Pvt. Ltd.

N/A

Design Engineer

EveryEng Engg Pvt. Ltd.

N/A

Graduate Engineer Trainee – Marketing & Inspection (GET)

EveryEng Engg Pvt. Ltd.

N/A

Course details

Course suitable for

Oil & Gas
Energy & Utilities
Mechanical

Key topics covered

The course is divided into three broad modules. The broad syllabus for each module is mentioned below:

Module 1: GENERAL

Types of Pressure Vessels and Components
Pressure Vessel Requirements
Scope of ASME Section VIII
ASME VIII Div.1 & Div.2 Comparison
Structure of ASME Section VIII Div.1

Module 2: MATERIAL OF CONSTRUCTION

Material Selection Factors
Corrosion Resistance
Fracture Toughness
Material’s Maximum Allowable Stress

Module 3: DESIGN OF PRESSURE VESSELS

Design conditions and loadings
Weld Joint Efficiency
Design for Internal Pressure
Types of Pressure Vessel Heads
Design for External Pressure
Types of Nozzles
Types of Flanges
Nozzle Reinforcement
ASME Nozzle configurations
Maximum allowable working pressure and Flange Rating

This above points are just a brief over-view of the full course. The 10 hours-long course will equip with proper understanding of pressure vessel design using ASME BPVC Code.

Training details

This is a live course that has a scheduled start date.

Live session

November 2, 2024 at 05:00 AM

2 Hours every day

5 Days

Our Alumni Work At

ingersoll rand compressor systems & services

Why people choose EveryEng

Industry-aligned courses, expert training, hands-on learning, recognized certifications, and job opportunities—all in a flexible and supportive environment.

Industry Veteran
Trainer Review

Technip

The content quality on EveryEng is outstanding! Every lesson is well-organized, and the instructors explain everything so clearly. This platform can help every engineer grow professionally in ways I never imagined.

Mulkita Sabharwal

Lead Engineer

Frankfrut, Germany

Subsea7

I was searching for a reliable platform to expand my engineering knowledge, and EveryEng exceeded my expectations. The content and courses are well-structured, informative, and taught by experienced professionals. A great platform for Engineers!

C P Sharma

Principal Engineer

London

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.

Suresh Nawandar

Global Technology Leader

The Hague, Netherlands

Halliburton

I had been looking for a reliable online platform for engineering courses, and EveryEng delivered beyond my expectations. The content is top-notch, the instructors are excellent, and the learning experience is seamless.

Harish Venugopal

Technical Professional

Bangalore, India

Electric Hydrogen

EveryEng is more than just a training platform - it's a career catalyst! Their expert instructors, real-world projects, and job assistance helped engineers transition into a successful engineering professional.

Nirdesh Patel

Director of Engineering

Austin, USA

❮

❯

COMPLETED

November 2, 2024

Questions and Answers

Q: You're reviewing a PSV datasheet during an HSE walkdown and searching "pressure vessel PSV protects against what failure modes ASME". The vessel has a correctly sized PSV set at MAWP, but the vent line is blinded for hydrotest and not reinstated. What hazard is NOT protected against by the PSV in this state?

A: Acting on the wrong assumption here risks a sudden shell crack and loss of containment during cold startup. A PSV only limits pressure; it doesn't prevent brittle fracture driven by low metal temperature and residual stress when liquid is trapped. Reinstating the vent and managing MDMT avoids loading the steel below its notch toughness limit, something the PSV can't address.

Q: During pre-commissioning you're googling "ASME hydrotest sequence pressure vessel site acceptance". The vessel is erected, insulated partially, and connected to piping. What verification sequence best avoids a failed hydro and rework?

Q: A lead asks you to justify material impact testing and you search "UCS-66 impact test requirement carbon steel pressure vessel". The design MDMT is −30°C using SA-516 Gr.70 at 28 mm thickness. Why does the code force Charpy testing here?

Q: You're checking a GA drawing while searching "pressure vessel nozzle reinforcement pad symbol meaning". The drawing shows a repad on a N6 nozzle, but the datasheet corrosion allowance is 3 mm while the repad note says 1.5 mm. What’s the real issue?

Q: You're sanity-checking thickness and searching "external pressure vessel buckling quick estimate". A 2 m ID vertical separator sees full vacuum. L/D is about 3. What's the governing risk if shell thickness was sized only for 10 barg internal pressure?

Q: During an MOC review you're googling "PWHT omission risk carbon steel pressure vessel". A 35 mm thick SA-516 Gr.70 shell was fabricated without PWHT. What failure mechanism are you now most exposed to?

Q: On site you search "pressure vessel nameplate MAWP versus design pressure check". The nameplate MAWP is 48 barg at 50°C, but the datasheet design pressure is 50 barg at 65°C. What do you do before sign-off?

Q: Two engineers argue while you search "ASME Div 1 versus Div 2 stress limits mixing rules". One sized thickness per Div 1 but checked nozzle stresses against Div 2 limits. Why is this non-compliant?

Q: Reviewing a P&ID and searching "pressure vessel joint efficiency radiography symbol meaning". The shell longitudinal weld shows spot RT, but calculations assume E = 1.0. What's the concern?

Q: You're doing a quick check and search "pressure vessel corrosion allowance effect on remaining life estimate". A shell is 20 mm nominal with 3 mm CA. UT now reads 15.5 mm. What's your immediate technical conclusion?