Process Safeguarding - Safety in Process Design

Atharva Proctek
In Pune

Price on request
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Important information

  • Training
  • Pune
  • Duration:
    5 Days
  • When:

This program is for ensuring the layout the procedure is secure, adhere to worldwide standard.
Suitable for: This  program is for  those student who have done Chemical engineering, process engineering, rotating equipments engineering, instrument engineering, project manager, maintenance engineering, operations engineering.

Important information

Where and when

Starts Location
Atharva Proctek,Karvenagar, PUNE, 411052, Maharashtra, India
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Frequent Asked Questions

· Requirements

For doing this particular program student should have done: Chemical engineering, process engineering, rotating equipment engineering, instrument engineering, P.M., maintenance engineering, operations engineering.

Course programme

Program Aim:

The teaching includes various topics of the safeguard processing. The topic includes different function in hydrocarbon & Chemical process. The title itself explains the processing of the tools & unit. The processing designing safe direction of the candidates consequences in safe processing designing.


* Synopsis of process designing of P&I layouts & different process system
* Intro

Basic Concepts

** Pressure in Processing Designing & Mechanical Pressure System Designing

** Pressure in Designing of relief System or tools

** Temp. in layout

** Temp. & Pressure vs. Mechanical layout of a Pressure container

** Decisive the Pressure Systems

** Decisive the Design Pressure (Upper Designing Pressure)

Common Values of protective against Over-pressure

** Immediate incidence of Over-pressure Cases

** Consequence of Operator reply

**Over-pressure safeguard by tools

**The function of Check Valve (Non-Return Valve)

**The function of Lock System on Block Valve

**The consequence of Automatic Control

* Explanation of final safeguard fundamentals

Purpose of Individual Relief Case

** Electrical Power Fail

** Sum Cool Water Fail

** Total Instrument Air Fail

** Involuntary Valve Open

**Block Outlet

**Other Fail

** Fire

** Thermal Expansion

De-pressure System

**E.D.P. System

** Depressure System for Process Safeguard or Operating cause

** Emergency Depressure rates versus A.P.I. 521 rules

Safeguard by Tool

** Categorization & execution of tools protective task

** Example of I.P.F. initiate basics

* Interface with other plant or plant section
* Pressure respite & disposal system

Pressure Relief Devices

**Meaning of conditions

**Kinds & size of Pressure Relief Device

**Synchronization of Pressure Relief Valve

Disposal System

**Flare System

**Vent to Atmospheric.

**Removal Back into Processing or Storaging

* Safeguard memo & Process safeguard flow diagram
* Computation measures

Estimate of Flow through Controlled Valve & Globes Valve

**Controlled Valve

**Globes Valve

**Prelim. Estimation of the mass of Controlled Valve & Bypass Valve

Estimate of Potential Pressure Wave during Heat Exchanger Tubes Rupture

Estimate of Flow from a Ruptured Tubes

Size of De-pressure Valve


**System Inventory

**Vapor from Liquid Vaporization by Fire

**Vapor from Liquid Flash due to De-pressure

**Estimate of Vapor Produce by Fire & Liquid Flash

**Vapor from Density Changed

**Estimation of the Initial De-pressure Flow Rate & Size of the Valve

* Low temp. Considerations during de-pressure

**Low Temp. in toolbeing Depressure

**Low Temperatures in Depressure Valve & downstream Pipe during


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