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Unlock P&ID Preparation Guidelines and Common Practices

سرفصل های دوره

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


1. Introduction
  • 1. Introduction
  • 2. Details shown on a P AndID VS a PFD
  • 3. Project Workflow and the Role of a P AndID within a Project
  • 4. Anatomy of a P AndID Drawing

  • 2. Details Shown on a P AndID
  • 1. Equipment Arrangement Series VS Parallel VS Spare
  • 2. Equipment Design Data And Specifications
  • 3. Examples for Equipment Data Tables on a P AndID
  • 4. Scope and Battery Limits

  • 3. Piping Details on a P AndID
  • 1. Analyzing Pipe Details on a Line Number
  • 2. Showing Fittings on a P AndID Reducers, enlargers, Class Breaks And Insulation Kits
  • 3. Manual Valves
  • 4. Check Valves
  • 5. Data Not Shown on a P AndID

  • 4. Instrument, Control and Shutdown Details
  • 1. Components of Control and Shutdown Loops
  • 2. Main Instrument Abbreviations on a P AndID
  • 3. Details of Measuring Devices
  • 4. Flow Measurment
  • 5. Level Measurement
  • 6. Temperature and Pressure Measurement
  • 7. Control System
  • 8. Shutdown System
  • 9. Types of Final Elements
  • 10. Control Valves
  • 11. Shutdown Valves
  • 12. On Off Valves Control in Batch Systems
  • 13. Valve Actuators and Accessories
  • 14. Motor Details

  • 5. Relief Devices
  • 1. Showing Pressure Safety Valves (PSV)
  • 2. Tank Protection Using Pressure Vacuum Safety Valves (PVSV)

  • 6. P AndID Stages within a Project
  • 1. Main P AndID Issuance Purposes
  • 2. Conceptual and Basic Engineering
  • 3. Issuing P AndIDs for Design
  • 4. HAZOP Session and Its Effect on a P AndID
  • 5. Construction and As-Built P AndIDs
  • 6. Effect of Changes in a P AndID on a Project Workflow

  • 7. Types of P AndIDs
  • 1. Legend P AndIDs
  • 2. Typical Details P AndIDs
  • 3. Distribution P AndIDs
  • 4. Tie-in P AndIDs
  • 5. Main Process Considerations when selecting Tie-in Location
  • 6. Packaged P AndIDs

  • 8. Performance Indication on a P AndID
  • 1. How to Provide the Operator with Plant Performance Indicators
  • 2. Measuring reading from Field using Field Instruments
  • 3. Show Instrument Reading to Operator in Control Room
  • 4. Warn the Operator from Upset Conditions Using Alarms
  • 5. Sampling Connections from the Plant to the Laboratory

  • 9. Plant Maintenance Isolation Techniques
  • 1. Importance of Plant System Isolation
  • 2. Types of Isolation
  • 3. Factors to choose Isolation Technique
  • 4. Isolation of pumps
  • 5. Isolation of Vessels and Shell And Tube Exchangers
  • 6. Isolation of Control Valves
  • 7. Isolation of Pressure Safety Valves (PSVs)

  • 10. Maintenance of Static Equipment
  • 1. Preparation for Static Equipment Maintenance
  • 2. Steaming out a Vessel

  • 11. Equipment and Piping Drainage
  • 1. Choose the Drainage Location
  • 2. Closed Drain System
  • 3. Open Drain System

  • 12. Introduction to P AndID Process Safety Considerations
  • 1. Potential Hazards in a Process Plant
  • 2. Warn the Operator - Layers of Protection
  • 3. Proper Design Conditions - Eliminate the Risk
  • 4. Fail Safe Position - Eliminate the Risk
  • 5. Prevent Hazard by Shutting down the System - Layers of Protection
  • 6. Mitigate Hazard by PSV - Layers of Protection

  • 13. Choose the Proper Design Conditions
  • 1. Design Pressure of Centrifugal Pump Discharge System
  • 2. Design Temperature for the system downstream a Cooler
  • 3. Applying 10 13 Rule on a shell And Tube Exchanger to handle Tube Rupture Scenario
  • 4. Compressor Settling Out Pressure
  • 5. Design Temperature of Compressor Suction

  • 14. Valve Fail Safe Position
  • 1. Control Valve Fail Action a in High to Low Pressure Interface
  • 2. Valve Fail Action in Reactor Cooling System
  • 3. Control Valve Failing in Location

  • 15. Plant Protection using Shutdown Actions
  • 1. External Equipment Protection from Process Upsets
  • 2. Avoid Common Cause Failure by Segregation between Control and Shutdown Systems
  • 3. Gas Blowby Example

  • 16. Protection using PSV and its Sizing Cases
  • 1. Reciprocating pump discharge, Pipe Thermal Expansion And Exchanger Tube Rupture
  • 2. Blockage, External Fire, Control Valve Failure, and Coolant Failure
  • 3. How to Properly choose the PSV Sizing Cases

  • 17. Plant Depressurization and Blowdown
  • 1. Purpose of Automatic Depressurization
  • 2. Configuration of Blowdown System
  • 3. Depressurization Timing Criteria
  • 4. Dividing Plant into Sections

  • 18. Relief System Considerations
  • 1. What is a Flare System
  • 2. Considerations for Inlet Pipe to PSVs
  • 3. Outlet PSV line Considerations
  • 4. Calculating Relief Load of Flare Header

  • 19. Assessing P AndID Protection Measures with HAZOP Session
  • 1. Role of Safety Studies
  • 2. Main HAZOP Rules
  • 3. Node Classifications
  • 4. Example of HAZOP Worksheet
  • 5. Example 1 No Flow Deviation at Vessel Inlet
  • 6. Example 2 More Liquid Flow to Vessel
  • 7. Analysis and Recommendations for Example 2
  • 8. Example 3 More Gas Flow to Vessel
  • 9. Example 4 Less Liquid Level in the Vessel

  • 20. SIL Assessment of Process Safeguards
  • 1. What is SIL Assessment
  • 2. How to Assess Frequency of a Hazard Consequence
  • 3. Analyse the severity of a Consequence
  • 4. Applying Risk Reduction Matrix
  • 5. Example 1 HIPPS system to protect Vessel Inlet
  • 6. Example 2 Protection against Gas Blowby
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    تاریخ انتشار: ۱۳ مرداد ۱۴۰۲
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