Apply Hazop, Sil & Process Safety Practices On P&Id Design

Analyze layers of protection of equipment, piping, and system against safety and operational issues by HAZOP & SIL study

What you'll learn

P&ID guidelines for Process Safety

Analyze plant layers of protection

Warn the Operator to respond against upsets through Alarms

Prevent Hazard by Process / System Shutdown

Mitigate Hazard using Process Safety Valves

Proper Equipment Design Conditions to Ensure Inherently Safe Operation

Control and Shutdown Valve Fail Safe Positions

HAZOP and SIL Assessment of a P&ID

Requirements

Basics of P&IDs

Description

Are you passionate about ensuring the safety and reliability of industrial processes? Do you want to master the art of safeguarding piping, equipment, and systems against unforeseen challenges and process upsets? If so, our comprehensive course on process safety is your key to success.Course Highlights:Understand the vital role of process safety in industrial settings.Explore methods to protect your plant against a wide range of scenarios, from power failures to fire incidents.Learn how to incorporate safety measures into Piping and Instrumentation Diagrams (P&IDs).Discover how to specify the proper design pressure and temperature of our equipment, piping, and systems.Explore the layers of protection, including alarms, shutdown systems, and pressure safety valves (PSV), in preventing process upsets.Delve into the world of Hazard and Operability (HAZOP) study and understand how it's conducted on a P&ID to enhance process safety.Dive into Safety Integrity Level (SIL) analysis and how to ensure that our layers of protection are addressing potential process deviations through a risk assessment related to the hazard severity and likelihood (frequency).Our engaging course includes video lectures, practical examples, quizzes, and interactive discussions. You'll have the opportunity to apply your knowledge to real-world scenarios.Ready to discover the realm of Process Safety? Enroll Now!Secure your spot and join us in ensuring safer industrial processes for a sustainable future. Don't miss this opportunity to master process safety and take your career to new heights.

Overview

Section 1: Introduction

Lecture 1 Introduction

Section 2: Layers of Protection

Lecture 2 Warn the Operator

Lecture 3 Proper Design Conditions - Eliminate the Risk

Lecture 4 Fail Safe Position - Eliminate the Risk

Lecture 5 Prevent Hazard by Shutting down the System - Layers of Protection

Lecture 6 Mitigate Hazard by PSV - Layers of Protection

Section 3: Choose the Proper Design Conditions

Lecture 7 Design Pressure of Centrifugal Pump Discharge System

Lecture 8 Design Temperature for the system downstream a Cooler

Lecture 9 Applying 10 13 Rule on a shell & Tube Exchanger to handle Tube Rupture Scenario

Lecture 10 Compressor Settling Out Pressure

Lecture 11 Design Temperature of Compressor Suction

Section 4: Valve Fail Safe Position

Lecture 12 Control Valve Fail Action a in High to Low Pressure Interface

Lecture 13 Valve Fail Action in Reactor Cooling System

Lecture 14 Control Valve Failing in Location

Section 5: Plant Protection using Shutdown Actions

Lecture 15 External Equipment Protection from Process Upsets

Lecture 16 Avoid Common Cause Failure by Segregation between Control and Shutdown Systems

Lecture 17 Gas Blowby Example

Section 6: Protection using PSV and its Sizing Cases

Lecture 18 Showing Pressure Safety Valves (PSV)

Lecture 19 Tank Protection Using Pressure Vacuum Safety Valves (PVSV)

Lecture 20 Reciprocating pump discharge, Pipe Thermal Expansion & Exchanger Tube Rupture

Lecture 21 Blockage, External Fire, Control Valve Failure, and Coolant Failure

Lecture 22 How to Properly choose the PSV Sizing Cases?

Section 7: Relief System Considerations

Lecture 23 What is a Flare System?

Lecture 24 Considerations for Inlet Pipe to PSVs

Lecture 25 Outlet PSV line Considerations

Lecture 26 Calculating Relief Load of Flare Header

Section 8: Plant Depressurization and Blowdown

Lecture 27 Purpose of Automatic Depressurization

Lecture 28 Configuration of Blowdown System

Lecture 29 Depressurization Timing Criteria

Lecture 30 Dividing Plant into Sections

Section 9: Assessing P&ID Protection Measures with HAZOP Session

Lecture 31 Role of Safety Studies

Lecture 32 HAZOP Session and Its Effect on a P&ID

Lecture 33 Main HAZOP Rules

Lecture 34 Node Classifications

Lecture 35 Example of HAZOP Worksheet

Lecture 36 Example 1: No Flow Deviation at Vessel Inlet

Lecture 37 Example 2: More Liquid Flow to Vessel

Lecture 38 Analysis and Recommendations for Example 2

Lecture 39 Example 3: More Gas Flow to Vessel

Lecture 40 Example 4: Less Liquid Level in the Vessel

Section 10: SIL Assessment of Process Safeguards

Lecture 41 What is SIL Assessment?

Lecture 42 How to Assess Frequency of a Hazard Consequence?

Lecture 43 Analyse the severity of a Consequence

Lecture 44 Applying Risk Reduction Matrix

Lecture 45 Example 1: HIPPS system to protect Vessel Inlet

Lecture 46 Example 2: Protection against Gas Blowby

Chemical Engineering students and fresh graduates,Process Engineers looking for enhancing their P&ID Preparation Skills,Plant Operation Engineers willing to understand the behind-the-scene concepts of plant design and share solutions to enhance the safety and operability of your plant.,Non-Process Engineers for example, instrumentation or mechanical engineer who wants to understand the criticality of process engineering requirements and how your role affects the plant performance