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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