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Pressure Relief Devices Masterclass (Asme Bpvc / Api Rp520)

Posted By: ELK1nG
Pressure Relief Devices Masterclass (Asme Bpvc / Api Rp520)

Pressure Relief Devices Masterclass (Asme Bpvc / Api Rp520)
Published 5/2024
MP4 | Video: h264, 1920x1080 | Audio: AAC, 44.1 KHz
Language: English | Size: 2.88 GB | Duration: 8h 0m

Design, Sizing, Selection, Installation and Operation of Safety Valves, Pressure Relief Valves and Rupture Discs

What you'll learn

Learn from WR Training industrial experts what they wrongly calculated during project startup, debottlenecking and commissioning

Understand safety valve manufacturers’ literature better and understand their jargon

Understand rupture disc manufacturers’ literature better and understand their jargon

Understand how the ASME Boiler and Pressure Vessel Code, Section VIII affects sizing, selection, assembling, testing and installation of pressure relief devices

Understand how the API Recommended Practice RP520 affects sizing, selection, assembling, testing and installation of pressure relief devices

Become more aware of the potential benefits and pitfalls of the currently available safety valves and rupture discs technology

Size and select pressure relief devices according to the currently available state-of-the-art sizing technology

Make more informed and creative decisions in the selection, sizing, installation and use of safety valves and rupture discs and their applications

Test your knowledge with +150 question-quiz

Download useful technical data covering terminology, standards, codes, basic design, sizing and selection information

Requirements

The student who will gain the most from this course will come equipped with some knowledge of fluid systems and an acquaintance with process valves. For these reasons, we strongly recommend that prior to taking the present course, you attend first our courses :

1. Valves : Principles, Operation & Design

2. Flow of fluids through piping systems, fittings, valves and pumps

3. Designing piping systems : Pipe, fittings, flanges and valves

Please note that the mathematics in this course is undemanding. All the work can be done with a hand-held calculator with powers, roots and log functions.

Description

Safety valves, pressure relief valves and rupture discs should be taken very seriously.They must always accurately respond to system conditions and prevent catastrophic failure when other instruments and control systems fail to adequately control process limits.Unfortunately, because of the lack of knowledge and disappearing expertise worldwide, the quality of selection and operation of these pressure relief devices is often insufficient.This possibly jeopardizes the safety of each of us, living or working in the neighborhood of a process plant.Proper sizing, selection, manufacture, assembly, test, installation and maintenance of a safety valves, a pressure relief valve or a rupture discs are all critical to obtaining maximum protection.Designed around a series of practical examples which we work through to a solution, this valuable course is an essential guide to a complete understanding of construction details and functioning of safety valves, pressure relief valves and rupture discs.This understanding is a pre-requisite for the proper sizing, selection, assembly, test, installation and maintenance of pressure relief valves.The course presents reference data, technical recommendations and field observations based on our many years of experience in sizing, selecting, testing, installing and operating pressure relief devices.The basic formulae and capacity correction factors contained in this course reflect current state-of-the-art pressure relief devices sizing technology.Typical valve sizing examples have been included to assist in understanding how specific formulae are applied.Useful technical data covering terminology, standards, codes, basic design, sizing and selection information, are presented in an easy to use format.Reference is made to :ASME Boiler and Pressure Vessel Code (BPVC), Section VIII, Pressure Vessels API Recommended Practice RP520This course also cautions the piping designer, the process engineer and any user of safety valves, that the performance of a properly sized and selected pressure relief device, can be severely compromised when used in conjunction with improper companion piping or incorrect handling and installation.Pressure relief device installation guidelines and their rationale, as well as some precautions, are offered to ensure optimum performance and safety.Now, while it is obviously impossible to address every installation mistake ever made, we have included a valuable summary of the most frequent installation mistakes encountered in the field.In addition, you will find at the end of each section a technical quiz to help you test your knowledge.If you pass wonderful, if not, you can watch the video lectures again or ask us for help in the Q&A section.We are confident that this valuable course will help you contribute to the safety of your facility, your fellow workers and yourself.Thank you for watching. Hope to see you there.WR TrainingSpread the wings of your knowledgeIMPORTANT SAFETY NOTESIt is important to always remember that a safety valve, a pressure relief valve or a rupture disc is a safety device employed to protect pressure vessels or systems from catastrophic failure. With this in mind, the application of pressure relief devices should be assigned only to fully trained personnel and be in strict compliance with rules provided by the governing Codes and StandardsPressure relief devices must be sized, selected and installed by those who have complete knowledge of:The pressure relieving requirements of the system to be protectedThe environmental conditions particular to that installationSafety valves, pressure relief valves and/or rupture discs sizing and selection is the responsibility of:The process engineerThe user of the system to be protectedSizing and selection of pressure relief devices should not be based on arbitrarily assumed conditions or incomplete information. Merely having a mandatory safety device installation does not make a system safe

Overview

Section 1: PART I Safety & Pressure Relief Valves - Design fundamentals

Lecture 1 Introduction

Lecture 2 Types of devices

Lecture 3 Useful terminologies

Lecture 4 Relief and Safety valves

Lecture 5 Safety valves

Lecture 6 Safety valves : Pressure setting

Lecture 7 Safety valves : 3D dismantling

Lecture 8 Safety valves : 2D dismantling

Lecture 9 Relief valves

Lecture 10 Relief valves : Valve operation in 2D cross-sectional view

Lecture 11 Relief valves : 3D dismantling

Lecture 12 Relief valves : 2D dismantling

Lecture 13 More on spring loaded design

Lecture 14 More on spring loaded design : 3D animation

Lecture 15 Material of construction

Lecture 16 Back pressure considerations

Lecture 17 Dynamic back pressure (built-up back pressure)

Lecture 18 Seat leakage

Lecture 19 Testing safety valves with air or nitrogen

Section 2: PART I Safety & Pressure Relief Valves - Codes and Standards

Lecture 20 Introduction

Lecture 21 API Codes and Standards

Lecture 22 ASME Codes and Standards

Lecture 23 ANSI Codes and Standards

Lecture 24 Other Codes and Standards

Lecture 25 Approval authorities

Lecture 26 Sizing safety valves : Heads-up

Lecture 27 Safety message

Section 3: PART I Safety & Pressure Relief Valves - Safety valves selection

Lecture 28 Introduction

Lecture 29 Setting and sealing

Lecture 30 Effect of back pressure on set pressure

Lecture 31 Pressure level relationships according to API RP520

Lecture 32 Safety valve positioning

Lecture 33 Example #1 : Positioning a steam application safety valve

Lecture 34 Example #2 : Positioning a process safety valve

Section 4: PART I Safety & Pressure Relief Valves - Safety valves sizing

Lecture 35 Keep in mind and always remember !

Lecture 36 Introduction

Lecture 37 Finding the fault flow

Lecture 38 Coefficient of discharge

Lecture 39 Sizing equations for steam 1/3 : General equation

Lecture 40 Example #3 : Sizing a safety valve for a steam application

Lecture 41 Sizing equations for steams 2/3 : Wet Steam

Lecture 42 Sizing equations for steams 3/3 : Dry Saturated Steam and Superheated Steam

Lecture 43 Example #4 : Sizing a safety valve for Superheated Steam

Lecture 44 Sizing for liquids and gases - Intro

Lecture 45 Required sizing data

Lecture 46 Sizing for gases : 10% Overpressure - Mass flow rate (lb/h)

Lecture 47 Sizing for gases : "C" coefficient

Lecture 48 Sizing for gases : "Kb" coefficient

Lecture 49 Sizing for gases : Compressibility factor

Lecture 50 Example #5 : Atmospheric back pressure

Lecture 51 Example #6 : Constant superimposed back pressure

Lecture 52 Example #7 : Set pressure below 30 psig

Lecture 53 Example #8 : Variable superimposed back pressure

Lecture 54 Sizing for gases : 10% Overpressure - Standard Volumetric flow rate (scfm)

Lecture 55 Example #9 : Variable built-up back pressure

Lecture 56 Sizing for liquids

Lecture 57 Sizing for liquids : "Kw" coefficient

Lecture 58 Sizing for liquids : "Kv" coefficient

Lecture 59 Example #10 : Sizing for a non-viscous liquid application

Lecture 60 Example #11 : Sizing for a viscous liquid application

Lecture 61 Multiple valve sizing

Lecture 62 Noise level calculations

Lecture 63 Noise intensity

Lecture 64 Example #12 : Noise level calculations

Lecture 65 Sizing for vaporizing liquids - Fire conditions

Lecture 66 Logic diagram for effective liquid level calculation

Lecture 67 Example #13 : Sizing for fire conditions (liquids)

Lecture 68 Sizing for gases and vapors only - Fire conditions

Lecture 69 Example #14 : Sizing for fire conditions (gases and vapors only)

Lecture 70 Capacity conversion

Lecture 71 Example #15 : Converting a propane PRV

Section 5: PART I Safety & Pressure Relief Valves - Safety valves installation

Lecture 72 Introduction

Lecture 73 Piping connection

Lecture 74 Excessive pressure drops

Lecture 75 Isolation valves

Lecture 76 More on piping connection

Lecture 77 Calculating piping losses

Lecture 78 Entrance effects

Lecture 79 Piping inlet losses

Lecture 80 Upstream devices

Lecture 81 Example #16 : Evaluating existing safety protection

Lecture 82 Calculating outlet piping

Lecture 83 Example #17 : Calculating discharge piping diameter

Lecture 84 Reaction forces

Lecture 85 Frequent installation mistakes

Section 6: PART II Rupture & Bursting Discs - Introduction

Lecture 86 Introduction

Lecture 87 What is a rupture disc ?

Lecture 88 How are rupture discs used ?

Lecture 89 Useful terminologies

Lecture 90 Useful terminologies - part II

Lecture 91 Types of rupture discs

Lecture 92 Rupture disc and holder assemblies

Lecture 93 Welded cartridges

Lecture 94 Selecting a rupture disc

Lecture 95 Manufacturing Design Range (MDR)

Lecture 96 Additional selection criteria

Lecture 97 How long will a rupture disc last ?

Lecture 98 Troubleshooting

Section 7: PART II Rupture & Bursting Discs - Rupture disc sizing

Lecture 99 Introduction to rupture disc sizing

Lecture 100 Overpressure allowance

Lecture 101 Sizing methodologies

Lecture 102 The coefficient of discharge method - Part I

Lecture 103 Sizing example #1 - Gases and vapors other than steam

Lecture 104 The coefficient of discharge method - Part II

Lecture 105 Sizing example #2 - Gases and vapors other than steam

Lecture 106 The coefficient of discharge method - Part III

Lecture 107 Sizing example #3 - Superheated steam

Lecture 108 The coefficient of discharge method - Part IV

Lecture 109 Sizing example #4 - Viscous liquids

Lecture 110 Resistance to flow method (KR)

Lecture 111 Sizing example #5 - Vapors using KR values

Lecture 112 Sizing example #6 - Liquids using KR values

Lecture 113 For more details

Section 8: PART II Rupture & Bursting Discs - Rupture disc / relief valve combination

Lecture 114 Introduction

Lecture 115 Combination Capacity Factor (CCF)

Lecture 116 Applying the CCF

Lecture 117 Sizing example #7 - Sizing combination devices

Section 9: PART II Rupture & Bursting Discs - Installation and maintenance of rupture discs

Lecture 118 Installation

Lecture 119 Holder preparation

Lecture 120 Rupture disc preparation

Lecture 121 Installing a rupture disc

Lecture 122 Assembly installation

Lecture 123 Inspection

Section 10: PART II Rupture & Bursting Discs - More on rupture disc KR values

Lecture 124 The "UD" ASME Code Stamp

Lecture 125 What does KR mean ?

Lecture 126 How do I use KR ?

Lecture 127 What impact will KR have on my system ?

Lecture 128 Where can I find KR for my rupture disc ?

Section 11: PART II Rupture & Bursting Discs - Final thoughts

Lecture 129 Final thoughts

Chemical, Process, Petroleum Engineers,Design Engineers,Piping Engineers,Plant Engineers,Plant operators,Mechanics,Safety professionals,Pressure vessels and piping inspectors