
Understanding the principle behind Process Safety discipline and its importance are the main things for you to consider in introduction. This lesson covers:
The question of "What is Process Safety?";
Difference between Process and Personal Safety and
What minor failings can lead to a major accident
The core and most fundamental element of Process Safety is the combination of hazard and risk terms that stands at the center of hazard identification. This session aims to give you brief information about:
What is hazard/risk?;
Auto Ignition Temperature;
Chemical and Physical Hazards and
Hazard Identification Techniques
The Risk Management Process is the key to reaching out safe process conditions that can be carried out both qualitatively and quantitatively. In this lecture, we will go over:
Determination of quality of hazard;
Oversimplifying assumption and
Qualitative Risk Assessment Techniques (HAZOP, What-If and etc.)
The initial step in risk management process is scenario development or going over the possible hazard scenarios to define the failure modes. This lesson aims to deliver brief information about:
Scenario development and Barrier Model;
Sources of Failures and
Limits affecting identification
The second step coming after scenario development is Consequence Analysis which waits for the subsequent Likelihood Analysis to work together forming risk matrix. In this session you will learn about:
Steps in Analysis and
Importance of Consequence Modelling
The second step coming after scenario development is Consequence Analysis which waits for the subsequent Likelihood Analysis to work together forming risk matrix. In this session you will learn about:
Steps in Analysis and
Importance of Consequence Modelling
After having an overview about Consequence modelling and its steps, it might be better to implement the knowledge illustrated in previous lecture. In this lesson, we will work on:
Application of release and dispersion modelling
Fire is a burn of material in air when the released material and air are in sufficient proportions. As the fire is one of the most dangerous consequence, fire modelling should be carried out. This video covers:
Types of fires;
Auto ignition and
Ignition sources
After having an overview about Fire modelling and its steps, it might be better to implement the knowledge illustrated in previous lecture. In this lesson, we will work on:
Implementation of fire modelling on different types of fire and
Considering the question of "What if there is that fire?"
The third step coming after scenario development which waits for the subsequent Consequence Analysis to work together forming risk matrix. In this session you will learn about:
Evaluation of frequency
Robustness and Relevancy in likelihood analysis
Fault and Event tree analysis is the part of Likelihood Analysis being quantitative risk assessment technique where the input data for even tree is taken from fault tree and risk model is proposed. In this lesson, we will go through:
FTA methodologies and principles;
Things to be considered in FTA and
Specific example for Event tree
After having an overview about Fault & Even tree analysis and its steps, it might be better to implement the knowledge illustrated in previous lecture. In this lesson, we will work on:
Application of Fault and Even Tree Construction
Just think about the risk management configuration where we have developed a scenario, Consequence modelling and Likelihood analysis by the help of Fault & Event tree analysis. This lecture aims to present the brief information about:
Definition of risk;
Individual and societal risk and
Risk evaluation
In the first lecture of Process Safety perspectives in Engineering, you will learn about:
ISD (Inherently Safer Design) philosophy
4 key principles of ISD
Even if you don’t know how to tie a tie, you have to have information about bowtie as an engineer. This lesson teaches you:
Theory behind Bowtie diagram. Swiss cheese model
What Bowtie diagram is
Example related to Bowtie diagram
Haven’t you watched our first 2 lectures yet? In this lecture, we will quickly review them and will talk about:
Process Control and control hazards
Common control issues
Prevent, Control, and Mitigation Systems
Plant Layout is an important and critical aspect of chemical process industries operations, but it is rarely taught as a unit of chemical engineering courses. We covered valuable information in this lesson for you! Click, watch the video and enjoy the lesson covering:
Optimization of Plant layout using SLP (safety and loss prevention)
Plant Layout consideration
First lesson of "Process Safety in Operation" course provide information about:
Process Safety Management and its phases
4 “C” approach (Control, Communication, Co-operation, Competence)
Till here, if you aren’t aware of importance of Process Safety, you must not miss the last lecture, because we are going to give information about:
Texas incident
Key steps of Process Safety Performance
Process Safety Performance Indicators and near misses
Strategies of maintenance
The necessity of Overpressure Protection and utilization of Relief Systems is undeniable that also reveals the need for correct documentation if required. Referring to this, the first lecture will be dedicated to:
The question of "What is Pressure Relief?";
A Statistical Analysis on the need for the installation of relief devices;
Management of change in Risk Management;
Pressure Relief Life Cycle;
Why is documentation important? and
Minimum Documentation Requirements
The second step you need to go for is understanding the codes and standards that should be followed. Because the safer operation is directly related to them and they can be beneficial for carrying out the remarkable means of Relief Device and System Installation. In this lecture, we will go through:
Codes and Standards;
Why do we need them?;
Hierarchy of Regulations and
Legislation and International Standards
After getting into the details of API standards, you can give a turn to the design philosophies and methods where you will see the essential steps for relief device selection and sizing, as well as, various methods to deliver high quality operation. This session aims to deliver the comprehensive information about:
Concept of Overpressure Protection;
The comparison between Relief and Blow-down;
Typical Philosophy Contents;
Inherently Safer Design and 2M2S principle;
Safety Instrumented Systems (SIS) and
The comparison between SIS and Relief Systems
Everything goes well: You have got the introduction to the documentation, codes and standards and learned about the design philosophy and its contents, now in this session, we will get into the Relief Scenarios by looking through the following topics:
Relief Design Steps;
The definition of Pressure System;
Importance of Boundaries;
Identifying Relief Scenarios and
The principle called "Double Jeopardy"
After defining the possible relief scenarios, determining relief loads will become very essential where we have decided to put more information about Low Pressure Storage Tanks and their venting. Here in this lecture, you will learn the valuable information about:
API620 0-15 PSI Storage Tanks;
API620 0-2.5 PSI Storage Tanks;
Types of Roof Construction;
Steps in Tank Vent Sizing and
Overfilling and Vacuum Scenarios
Consideration of single or multi-phase flow within the equipment is one of the most important tips for appropriate relief device sizing. So that, this lecture is dedicated to Single and Multi-phase Flow Relief Sizing that comprises the following topics inside:
Sizing methods for single phase flow;
Sizing methods for multi-phase flow;
Flow types to consider and
Sizing steps
More practical topics are coming for you in this section where we start with the installation of the relief device. This is the first part of the installation as this procedure is quite detailed to describe. Here in this session, you will mainly be informed about Inlet and Outlet Piping and will get into the details of other following topics:
Piping Installation;
Excessive Inlet Pressure Losses;
Complicated Inlet Piping and
Outlet Piping
Let's turn to the second part for installation as this procedure is quite detailed to describe. Here in this session, you will mainly be informed about the location of PRV and installation problem and will get into the details of other following topics:
Location of Installed SRV;
Reaction Forces and Bracing and
Common Installation Problems
One more necessary steps that should be covered is Segregation in Flare and Venting Systems which takes an action after installation of relief device. In this session, you will go over:
Part of Segregation;
Hydrate Prediction Methods;
Stream Segregation and
Matrix for mixing
The Flare Header Design as one of the last significant may look like Consequence Modelling comprising almost the same steps in its design principle. In this part for Flare Header Design, you will mainly work with liquid removal and its dispersion that are delivered by the following topics:
Liquid Removal and General Requirements;
Liquid Residence Time;
Dispersion Modelling and
Thermal Radiation
The Flare Header Design as one of the last significant may look like Consequence Modelling comprising almost the same steps in its design principle. In this part for Flare Header Design, you will mainly work with flare types and the factors influencing them that are delivered by the following topics:
Types of Flares;
Factors influencing Flare Design;
Elevated and Ground Flare Systems;
Flare Gas Recovery System and
Smoke Control and Husa Correlation
The last topic you will need to go for understanding the overall concept in detail is depressurisation. This lecture will mainly focus on Relief Devices and Blow-down that is provided by the following topics:
Relief vs Blow-down Systems;
Emergency and Operational Depressurisation;
Depressurisation System Setup;
Depressurisation Calculations and
Blow-down Loads
Chemical/Process Safety Engineering BOOTCAMP provided by Velocis Solutions aims to deliver practical and useful information set for course takers. The course bundle includes three separate courses of Process Safety Fundamentals, Process Safety in Engineering and Operations and Overpressure Protection.
The course structure is designed by considering your approach and level about the topic, that is why you can commence the course with getting introduction to Process Safety Fundamentals. In this first section, you can directly get into the risk management process and comprehend the necessary steps to define risk within the practical sessions, such as:
Importance of Process Safety
Hazard, Risk, Hazard Identification
Qualitative Risk Assessment
Hazard Scenarios
Consequence Analysis and Modelling
Types of Fires and Explosions
Likelihood Analysis and Fault & Event Tree Analysis (FTA)
Defining Risk and Risk Matrix
After forming the solid background about Process Safety discipline, you can give a turn to the second section where you will be given with the implementation of Process Safety in Engineering and Operations by focusing on the risk management process and following chapters:
Inherently Safer Design
Bowtie Diagram and Protective Systems
Plant Layout
Introduction to Safety in Operations
Process Safety Performance
More practical section, Overpressure Protection will welcome you, after you have completed the first two sections where the course takers can take the huge benefits of the best practical knowledge that was proposed by referring to API standards. The valuable source of information is delivered to course takers by going over the section through:
Introduction to the course and documentation (API Standards)
Design Philosophies and Methods
Relief Scenarios and Scenario Selection
Types of Relief Devices, Conventional Spring Loaded, Balanced Bellow, Pilot Operated
Single-phase and Multi-phase Flow Relief Sizing
Relief Device Installation, Calculation of Blow-down Orifice
Segregation in Flare and Venting Systems
Flare Header Design
Emergency and Operational Depressurisation