Unlock P&ID Preparation Guidelines and Common Practices

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Boostrand Training,Boostrand PE

5:02:28

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1. Introduction

1. Introduction.mp4

04:34

2. Details shown on a P AndID VS a PFD.mp4

04:56

3. Project Workflow and the Role of a P AndID within a Project.mp4

04:57

4. Anatomy of a P AndID Drawing.mp4

03:18

2. Details Shown on a P AndID

1. Equipment Arrangement Series VS Parallel VS Spare.mp4

01:45

2. Equipment Design Data And Specifications.mp4

03:49

3. Examples for Equipment Data Tables on a P AndID.mp4

02:24

4. Scope and Battery Limits.mp4

02:12

3. Piping Details on a P AndID

1. Analyzing Pipe Details on a Line Number.mp4

03:38

2. Showing Fittings on a P AndID Reducers, enlargers, Class Breaks And Insulation Kits.mp4

07:14

3. Manual Valves.mp4

02:34

4. Check Valves.mp4

00:57

5. Data Not Shown on a P AndID.mp4

01:27

4. Instrument, Control and Shutdown Details

1. Components of Control and Shutdown Loops.mp4

01:31

2. Main Instrument Abbreviations on a P AndID.mp4

01:48

3. Details of Measuring Devices.mp4

02:22

4. Flow Measurment.mp4

03:43

5. Level Measurement.mp4

04:24

6. Temperature and Pressure Measurement.mp4

00:33

7. Control System.mp4

02:46

8. Shutdown System.mp4

02:36

9. Types of Final Elements.mp4

01:50

10. Control Valves.mp4

01:12

11. Shutdown Valves.mp4

01:41

12. On Off Valves Control in Batch Systems.mp4

01:37

13. Valve Actuators and Accessories.mp4

04:46

14. Motor Details.mp4

01:19

5. Relief Devices

1. Showing Pressure Safety Valves (PSV).mp4

05:21

2. Tank Protection Using Pressure Vacuum Safety Valves (PVSV).mp4

01:37

6. P AndID Stages within a Project

1. Main P AndID Issuance Purposes.mp4

02:33

2. Conceptual and Basic Engineering.mp4

04:09

3. Issuing P AndIDs for Design.mp4

03:40

4. HAZOP Session and Its Effect on a P AndID.mp4

02:51

5. Construction and As-Built P AndIDs.mp4

02:16

6. Effect of Changes in a P AndID on a Project Workflow.mp4

01:31

7. Types of P AndIDs

1. Legend P AndIDs.mp4

03:58

2. Typical Details P AndIDs.mp4

01:29

3. Distribution P AndIDs.mp4

02:20

4. Tie-in P AndIDs.mp4

01:53

5. Main Process Considerations when selecting Tie-in Location.mp4

03:19

6. Packaged P AndIDs.mp4

01:38

8. Performance Indication on a P AndID

1. How to Provide the Operator with Plant Performance Indicators.mp4

01:04

2. Measuring reading from Field using Field Instruments.mp4

02:34

3. Show Instrument Reading to Operator in Control Room.mp4

06:10

4. Warn the Operator from Upset Conditions Using Alarms.mp4

03:03

5. Sampling Connections from the Plant to the Laboratory.mp4

01:45

9. Plant Maintenance Isolation Techniques

1. Importance of Plant System Isolation.mp4

02:14

2. Types of Isolation.mp4

03:16

3. Factors to choose Isolation Technique.mp4

05:08

4. Isolation of pumps.mp4

02:37

5. Isolation of Vessels and Shell And Tube Exchangers.mp4

03:27

6. Isolation of Control Valves.mp4

02:40

7. Isolation of Pressure Safety Valves (PSVs).mp4

06:53

10. Maintenance of Static Equipment

1. Preparation for Static Equipment Maintenance.mp4

03:44

2. Steaming out a Vessel.mp4

02:24

11. Equipment and Piping Drainage

1. Choose the Drainage Location.mp4

02:06

2. Closed Drain System.mp4

05:33

3. Open Drain System.mp4

02:20

12. Introduction to P AndID Process Safety Considerations

1. Potential Hazards in a Process Plant.mp4

02:52

2. Warn the Operator - Layers of Protection.mp4

03:21

3. Proper Design Conditions - Eliminate the Risk.mp4

01:05

4. Fail Safe Position - Eliminate the Risk.mp4

01:03

5. Prevent Hazard by Shutting down the System - Layers of Protection.mp4

01:39

6. Mitigate Hazard by PSV - Layers of Protection.mp4

00:51

13. Choose the Proper Design Conditions

1. Design Pressure of Centrifugal Pump Discharge System.mp4

04:53

2. Design Temperature for the system downstream a Cooler.mp4

00:49

3. Applying 10 13 Rule on a shell And Tube Exchanger to handle Tube Rupture Scenario.mp4

02:41

4. Compressor Settling Out Pressure.mp4

03:20

5. Design Temperature of Compressor Suction.mp4

01:37

14. Valve Fail Safe Position

1. Control Valve Fail Action a in High to Low Pressure Interface.mp4

02:17

2. Valve Fail Action in Reactor Cooling System.mp4

00:40

3. Control Valve Failing in Location.mp4

01:57

15. Plant Protection using Shutdown Actions

1. External Equipment Protection from Process Upsets.mp4

03:37

2. Avoid Common Cause Failure by Segregation between Control and Shutdown Systems.mp4

02:39

3. Gas Blowby Example.mp4

03:29

16. Protection using PSV and its Sizing Cases

1. Reciprocating pump discharge, Pipe Thermal Expansion And Exchanger Tube Rupture.mp4

04:15

2. Blockage, External Fire, Control Valve Failure, and Coolant Failure.mp4

04:49

3. How to Properly choose the PSV Sizing Cases.mp4

02:18

17. Plant Depressurization and Blowdown

1. Purpose of Automatic Depressurization.mp4

02:02

2. Configuration of Blowdown System.mp4

04:35

3. Depressurization Timing Criteria.mp4

01:20

4. Dividing Plant into Sections.mp4

03:32

18. Relief System Considerations

1. What is a Flare System.mp4

01:42

2. Considerations for Inlet Pipe to PSVs.mp4

02:56

3. Outlet PSV line Considerations.mp4

02:16

4. Calculating Relief Load of Flare Header.mp4

03:38

19. Assessing P AndID Protection Measures with HAZOP Session

1. Role of Safety Studies.mp4

04:01

2. Main HAZOP Rules.mp4

01:45

3. Node Classifications.mp4

01:40

4. Example of HAZOP Worksheet.mp4

01:22

5. Example 1 No Flow Deviation at Vessel Inlet.mp4

09:38

6. Example 2 More Liquid Flow to Vessel.mp4

06:42

7. Analysis and Recommendations for Example 2.mp4

05:02

8. Example 3 More Gas Flow to Vessel.mp4

01:57

9. Example 4 Less Liquid Level in the Vessel.mp4

02:17

20. SIL Assessment of Process Safeguards

1. What is SIL Assessment.mp4

02:23

2. How to Assess Frequency of a Hazard Consequence.mp4

07:42

3. Analyse the severity of a Consequence.mp4

01:59

4. Applying Risk Reduction Matrix.mp4

02:44

5. Example 1 HIPPS system to protect Vessel Inlet.mp4

02:29

6. Example 2 Protection against Gas Blowby.mp4

07:08

Description

Discover the details, operation, maintenance, and safety guidelines of piping and instrumentation diagrams

What You'll Learn?

Workflow of P&ID issuance and its role in a project
Details shown on a P&ID for piping, fittings, instruments, scope definition, ...etc.
Anatomy of the P&ID and P&ID types
P&ID Guidelines to ensure easy Plant Operation, startup and performance indication
Isolation of equipment for maintenance
Plant Drainage System
Maintenance and Steam Out Requirements
Plant Depressurization and Blowdown
P&ID guidelines for Process Safety
Expected Plant Hazards and Upset Conditions
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

Who is this for?

Chemical Engineering Student Looking for Learning Practical Engineering Concepts

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, a piping or instrumentation or mechanical engineer who wants to understand the criticality of process engineering requirements and how your role affects the plant performance

What You Need to Know?

Basic Chemical Engineering Knowledge

More details

Description
What is this Course About?
Explore the details and structure of P&IDs, and gain practical knowledge of plant operation and maintenance in addition to the common safety practices.
Here, we are not just focusing on answering "how" questions. We are more concerned with answering the "why" questions. This course offers a valuable opportunity to expand your understanding of P&IDs and their importance in real-world applications.
Starting from reading and understanding P&IDs, we shall dive deeper into the reasons behind different guidelines and practices, providing valuable insights into their significance.
Course Overview
This course gives a clear understanding of essential topics related to Piping and Instrumentation Diagrams (P&IDs). Throughout this course, we delve into vital details that should be included in a P&ID, equipping you with the knowledge to interpret and analyze these crucial documents accurately.
We begin by exploring the common data shown for equipment, piping, instruments, control systems, shutdown systems, and pressure safety valves. In addition, we shall cover the anatomy and different types of P&IDs (e.g. legend, distribution and tie-in P&IDs), enabling you to comprehend various P&ID representations and apply them smoothly.
Operational and maintenance guidelines play a significant role in ensuring smooth process functioning. That's why we shall delve into isolation philosophies for equipment and maintenance requirements. You'll gain insights into the purpose of closed drain and open drain systems and understand the distinctions between them. Furthermore, we explore plant depressurization and blowdown requirements and their impact on the flare system.
The course emphasizes critical process safety requirements. We'll see the importance of specifying proper design pressures and temperatures for equipment and piping to ensure inherent plant safety. We'll also cover fail-safe positions for valves based on anticipated hazards and upset scenarios.
In situations where an inherently safe system cannot be achieved, we shall examine layers of protection for the plant, including operator intervention, prevention, and mitigation of hazards. Each layer is carefully considered when preparing P&IDs to enhance overall safety.
To assess the adequacy of protection measures, we explore Hazard and Operability (HAZOP) and Safety Integrity Level (SIL) assessments, supported by practical examples that deepen your understanding of these fundamental risk assessment techniques.
Join us on this comprehensive P&ID course and gain a profound understanding of these topics, equipping you with the knowledge and skills to effectively analyze, interpret, and implement P&IDs in diverse industries.
Who this course is for:
Chemical Engineering Student Looking for Learning Practical Engineering Concepts
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, a piping or instrumentation or mechanical engineer who wants to understand the criticality of process engineering requirements and how your role affects the plant performance

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Boostrand Training

Instructor's Courses

Boostrand Training is dedicated to introducing courses aiming to help chemical engineers start their career in Process Engineering. With a chemical engineering background and more than 8 years of experience as a process engineer in oil and gas projects, including in Refining, Petrochemicals, Gas Processing, and Oil Facilities, Boostrand Training hopes it can help new graduates understand how these projects work and how units are designed throughout my courses.Through coding knowledge, Boostrand Training also aims to introduce the concept of automation of tasks of a process engineer through tools that depend on programming.

Boostrand PE

Instructor's Courses

Boostrand PE is dedicated to introducing courses aiming to help chemical engineers start their careers in Process Engineering.With a chemical engineering background and more than 8 years of experience as a process engineer in oil and gas projects, including in Refining, Petrochemicals, Gas Processing, and Oil Facilities, Boostrand Training hopes it can help new graduates understand how these projects work and how units are designed throughout my courses.Through coding knowledge, Boostrand Training also aims to introduce the concept of automation of tasks of a process engineer through tools that depend on programming.

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