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Process Hazard

Analysis (PHA)

Training by: Syed Hassan Sultan Date: 17 March 2016

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PROCESS HAZARD

ANALYSIS (PHA)

TRAINING CONTENT:

Module 1: PHA in the context of PSM

Module 2: PHA Process Overview

Module 3: PHA Planning & Preparation

Module 4: PHA Execution-Hazard

Identification

Module 4a: Hazard & Operability Study

(HAZOP) Technique Overview

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Running business implies taking

risks….

Module 1: PHA in the

context of PSM

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Module 1: PHA in the

context of PSM

Operational risks cover a large portion of the entire risk portfolio that major corporations are facing on a day-to-day business

---Adopting an integrated approach to the Company Risk

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Portfolio---Module 1: PHA in the

context of PSM

Process Hazard Analysis (PHA) is applied to understand risks involved in the design, operation, and modification of processes that handle hazardous materials

Understanding of risks plays a central role as it drives effective risk management activities

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Module 1: PHA in the

context of PSM

The impact to company’s objectives varies depending on the risks

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Module 1: PHA in the

context of PSM

PHA mainly focus on risks associated with handling of hazardous material with

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Module 1: PHA in the

context of PSM

It’s necessary to recognize the final implications to the company

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Module 2: PHA Process Overview

A “Hazard” is commonly considered as the “potential for…”

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Module 2: PHA Process Overview

A “Hazard” is commonly considered as the “potential for…”

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Module 2: PHA Process Overview

Every PHA implementation follows 3 phases

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Module 2: PHA Process Overview

PHA Execution: Logical Steps

Key steps of the PHA execution depend on the defined scope and methodology to be applied. In general terms, three main logic steps can be identified for any PHA

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Module 2: PHA Process Overview

There is not a uniform consensus across industries and standards on the terminology describing risk management process steps

---Example of terminology from different

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standards---Module 2: PHA Process Overview

A Comprehensive PHA program encompasses a number of components which are interconnected to provide a

complete understanding of risks.

---Key relationship among different PHA components (Not

Exhaustive)---The Hazard Identification stage is one of the most important steps

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Module 3: PHA Planning

and Preparation

Careful preparation lays the groundwork for a successful study

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Module 4: PHA

Execution-Hazard Identification

Hazard identification is the first step in a systematic process which aims to improve the management of risk

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Module 4: PHA

Execution-Hazard Identification

A number of techniques can be used in the hazard identification

---Common Hazard Identification

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Methodologies---Module 4: PHA

Execution-Hazard Identification

Different techniques apply different logic to help identifying hazards

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Module 4: PHA

Execution-Hazard Identification

Different techniques apply different logic to help identifying hazards

• What if / Checklist review can enter the logic at any point in the cause & effect relationship

• FMEA begins with looking at the cause (failed regulator) & works toward defining the consequence (vessel rupture)

• HAZOP begins with deviation (high pressure), determines the consequence (vessel rupture), and then identifies potential causes (failed regulator) of the deviation

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Module 4: PHA

Execution-Hazard Identification

Potential Hazards:

---Five Hazard

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Categories---Module 4a: Hazard and

Operability Study (HAZOP)

A HAZOP is a group technique used to identify hazards and operability issues arising from process deviations from plant design intent

The technique is used to identify

Hazards (ways the system can fail leading to human loss/injury, asset damage or environmental impact

Operability (ways in which the system can fail

to perform as required)

• The approach is formal and systematic using a structured question and answer procedure to identify deviations from the intent of the design. • The study is performed by a team of people

familiar with the system design and operation, working under the guidance of a leader who is experienced in the HAZOP method.

• The leader systematically applies a set of specific guideword-parameters combinations to evaluation deviations in terms

of causes, consequence, safeguards.

• The team evaluates whether existing safeguards are adequate to protect from the identified scenario; if not a recommendation for improvement is raised.

• A recorder makes a detailed tabulation of the team discussion.

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Module 4a: Hazard and

Operability Study (HAZOP)

The team for a HAZOP is selected from the available staff who will need to be free of others duties for the period of the study

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Module 4a: Hazard and

Operability Study (HAZOP)

Process deviations result from the

combination of guidewords to

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Module 4a: Hazard and Operability Study (HAZOP)

HAZOP can also be applied to batch

processes, using Ad Hoc guidewords applied to “ACTION”

Guidewords Deviation

No Action not executed

More Of Too much of action

Less Of Too less of action

As well as Additional action executed although not required

Part Of Action partially executed

Other than Incorrect action

Before Action executed too early

After Action executed too late

Disordered Action executed in the wrong order / sequence

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Module 4a: Hazard and

Operability Study (HAZOP)

Select line or vessel

Define node & design intention of node

Select parameter & guide word

Develop meaningful deviation

Identify all possible causes for the deviation

List safeguards & protection available Describe consequences if all safeguards fail

Evaluate need for risk control recommendation

Start here for each process line and vessel

Repeat for all guide words & parameters

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Module 4a: Hazard and

Operability Study (HAZOP)

A number of criteria and approaches can be used by the HAZOP Leader to identify /select

the nodes. Here are the most frequent adopted:

• Process Flow Analysis: the leader follows the main flows from/to the different process equipment and lines

• Presence of Loops: the leader can follow process loops when selecting the sequence of the Nodes

• Complexity of Equipment: Node coincide with 1 single process equipment, including relevant inlet/outlet lines and relevant instrumentation.

• “Line by Line” Approach: assigning a Node to each of the main process line and equipment.

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COMMUN ITY EMERGENCY RESPONSE PLANT EMERGENCY RESPONSE MITIGATION PREVENTION

Module 4a: Hazard and

Operability Study (HAZOP)

Part of the team discussion should include the layers of protection which already exist and the extent to which they are adequate

CONTROL & MONITORING

PROCESS

• The team members need a good

knowledge of the plant to explain accurately the protections already in place

• The extent to which these are

considered adequate depends on the size of the risk posed by the hazard

• The discussion should refer to the basic

process control system as well as any engineering controls or administrative procedures which are in place

Layers of Protection

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Module 4a: Hazard and

Operability Study (HAZOP)

Examples of HAZOP Notes-How do you judge the quality?

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Module 4a: Hazard and

Operability Study (HAZOP)

It’s important to clearly write recommendation so that they can be actionable

--- Examples of “Good Quality” of recommendations

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---Module 4a: Hazard and

Operability Study (HAZOP)

---Inadequate Quality of HAZOP-Key

Factors---• Inadequate Study Time

• Inadequate Documentation • Inadequate Team Members • Incomplete Study

• Inadequate Team Guidance • Inadequate Facilities

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Q/A Session

PLEASE FEEL FREE

TO ASK!

References

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