212625045-hazop
TRANSCRIPT
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HAZOP STUDY
Sabic E&PM Process & Process Safety SectionMarch 2007
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HAZOP STUDY
1.0 INTRODUCTION
HAZOP stands for HAZARD AND OPERABILITY
The application of a formal, systematic, critical, rigorous
examination to the process and engineering intentions
of new & existing facilities to assess the hazard
potential of mal -operation or mal -function of
individual items of equipment & the consequential
effects on the facility as a whole.
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1.1 Hazards & Risks.
Hazard is a physical situation with the potential for
human injury, damage to property, damage to the
environment or a combination of these.
Risk is the likelihood of an undesirable event occurring
within a specific period or under specified circumstance.
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1.2 Hazard Studies & SABIC Project Gate Process
: Hazard Reviews/Studies part of Safety Management
System (SMS),
: To identify safety, health, environment, operating and
maintenance problems.
: New Projects, a number of studies in different stages.
: Each study also verifies recommendations of previous
study have been implemented.
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1.3 SABIC PROJECT GATE PROCESS1.0 Concept Rationalization & Pre-feasibility.
2.0 Feasibility Study and Venture Philosophy (Preliminary HSE Review-
PHA I)
3.0 Project Strategy & Execution Plan.
4.0 Design Basis Development (PHA II)
5.0 Basic Design and Appropriation (HAZOP-PHA III)
6.0 Detailed Design and Construction .7.0 Close Out and Reappraisal Phase (PSSR)
SABIC Project Gate Process: At Gate 5, Basic Design and appropriation,
a detailed HAZOP study is carried out.
The application of HAZOP at the correct stage in a project means that
problems are identified and can be rectified during detailed design.This results in substantial savings.
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1.4 Objectives of the Study: Identifies process hazards that could lead to safety
related consequences
: Identifies operability or product quality problems
: Identifies quality issues in design
: Identifies maintenance issues.: Recommend actions to minimise risks associated
with identified hazards or eliminate the Hazard
HAZOP is an identifying technique & is not intended as a
means of solving problems.
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1.5 Benefits of a Hazop Study
: Increased plant availability hence production
: Improved product quality
: Improved quality of working environment
: Reduced insurance premiums
: Minimises & controls changes to design
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1.6 Limitations of a Hazop Study
Hazop Study is not an infallible method for
identifying all possible hazards.
Quality of the Study depends on -
:Expertise and experience of the team
:Accuracy and extent of information available
:Clear definition of scope of study
:Duration of the study:Good knowledge of the system
:Creativity of the team members
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1.7 Scheduling a Hazop Study
Prerequisites :
- Design must be well developed and firm.
- Drawings must be well prepared.
- Sufficient vendor information must be
available.
- Study must not be delayed too long.
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1.8 Applicable Systems
New designs.
Modification of existing Operations.
Repeat designs.
Existing Plants.Computer controlled processes.
Operating Procedures.
Pilot Plant and Laboratory processes.
Drains, vents and tie-in between Plants.
Commissioning and Decommissioning.
Emergency Operations.
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1.9 Basic Concept of HAZOP
Involves the splitting up of the plant (P & ID) into sections &the systematic application of a series of questions to each
section. The following terms are used as a basis for all
HAZOP studies:
Design intent - The way in which the plant is intended to operate.
Deviation - Any perceived deviations in operation from thedesign intent.
Cause - The causes of the perceived deviations
Safeguards - Existing provisions to mitigate the likelihood or
consequences of the perceived deviations &
to inform operators of their occurrenceActions -The recommendations or requests for information
made by the study team in order to improve the
safety and/or operability of the plant
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1.10 GuideWords& SystemParameters
Guide wordis an action word or phrase that assists the
team in a creative and thorough search for
meaningful deviations
:no, less, more, reverse etc.
System parameter is a variable, component or
activity associated with the stage under study
:flow, pressure, reaction, maintenance etc.
Not all Parameters apply to the study.
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HAZOP MATRIX
No Less More As well as Part of Reverse Other
thanFlow No flow Low flow High flow Misdirected Reverse
flow flow
Pressure Open to. Low pr. High pr. Vacuumatm.
Reaction No reaction Low react- High react- Side Incomplete Reverse Wrongion Rate ion rate reaction reaction reaction reaction
Vibration Low Highvibration vibration
Startup Incomplete Improperstart up start up
Mainte- Inability to Inadequate Additional Impropernance Maintain maintenance effort to mainte-
maintain nance
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1.11 Quantification
Whilst the HAZOP techniques was originally
conceived as a purely qualitative review, it can
be quantified to some extent by the use of
a simple ranking for likelihood & severity.
A typical likelihood ranking is as follows:1 Very Unlikely
2 Unlikely
3 Has happened once
4 Has happened a few times
5 Happens quite often
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A typical severity ranking is as follows :
1 Pollution
2 Minor injury/damage
3 Serious injury/damage
4 Fatalities/Major Damage5 Loss of installation
The two factors (Likelihood & Severity) can be
combined in a matrix to give an overall ranking
which can be used to prioritize actions.
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2.0 ORGANISING A HAZOP STUDY2.1 Scope of Study
. HSE issues?
. Operation, product quality & productivity issues?
. Maintenance, reliability, and Plant life ?
. Adherence to Company Policies & Procedures?
. Quality issues in Process design?
. Extended to Equipments and Machinery?
. Boundaries for the study?
. Problems beyond the boundaries be addressed?
. Hazop repeat designs or Hazopby difference?. Should non- steady state operations be included?
. Approach to Action Items or recommendations.
. How will redesign issues be handled?
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2.2 The Team- Study is only as good as the Team undertaking the study
- Composition dependent on Nature and complexity
- Expertise in basic disciplines and system operations
A typical team comprises:Chairman or Team leader,
Secretary/scribe,
Project Engineer,
Process Engineer,
Control and Instrument Engineer,Safety Engineer,
Operations Specialist (Lead Commissioning Engineer).
Other specialists may be consulted for specific points.
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2.3 Documents RequiredOperating and Control Philosophy doc. PFD, UFD, P&IDs
Material and Energy Balance Equipment specs
Vendor packages, Instrument specs
Relief / Venting philosophy Alarm and Trip settings
Material Safety Data Sheets Material reactivity dataDocs. of Hazards in similar systems Operating problems
Plot Plan Previous Safety Reports
Operation method (Batch Process)
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2.4 Recording the Proceedings
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3.0 HAZOP Study Procedure
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3.1 NodeSection of the Plant under Study; marked and no. on a P&ID.
Guidelines for creating Nodes
: Each Node should fit a clear Design Intention.
: Create a definitive conceptual model of the system.
: Control points or junctions of vessels.: Variation in Parameters as flow, pr., temp. & composition.
: In Batch Process, the sequential steps of operation.
Too many small Nodes
: Time consuming and expensive exercise.
: Analysis spills over to upstream and downstream sections.Too large a Node
: More than one Design Intention for the Node
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3.2 Node and its Design Intent
Description to include Operational range and Design Intent,
reference to equipments, to materials, conditions, source and
destination, to changes or transfers, to means of control and
timing of a step
3.3 Generate a Deviation
: Assign a Parameter, vary Guide Words.
: All combinations may not apply.Ex. - Higher Pressure.
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3.4 Identify the Causes
: All Causes to be identified before proceeding to next
step.
: Only realistic causes to be investigated. Quantitative Risk
Assessment (QRA) based on a combination of frequency ofevent and seriousness of the consequences.
: Include low frequency causeswith severe Consequences.
3.5 Evaluate Consequences
: Both immediate and delayed
: Both inside and outside the Node
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3.6 Categories for Consequences
S : Personnel Safety Impacted.ED : Equipment Damage.
BI : Business Interruption.
PRO: Loss of or Reduced Production.
E/H : Environment or Health Related.
Q : Product Quality Impact
3.7 Safeguards
Equipment or process feature(s) or procedural step(s), reducing the
likelihood of one or more Cause or severity of the
Consequence.
-Identify the worst Consequence and list Safeguard for this.-Be physically located within or directly applicable to the Node.
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3.8 Action Items: Adding hardware, providing interlocks, modifying
procedures or evaluating design adequacy.
: Only unanimously agreed solution(s)
: To be treated purely as recommendations of the Team.
: More effective protection could be available.: Suggested Action may not be feasible.
: Actions should be documented without ambiguity.
: For no action, write NoAction Required
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3.9 Remarks
Record any Remarks that will amplify the Deviation.
Ex : During normal operation, PIC-1 will limit flow
below set point of FIC-1.
: Valve CV changed from 300 to 400 to cope with
anticipated flow rate increase from 50K to 83K kg/h.3.10 Assign Responsibility in BYcolumn: Ex. - Client.
3.11 Record Status of Action Item in XcolumnBlank :Action item remains open for designated BYparty
C : Action completed with Comments
X : Action not required for Comments given.
R : Further Action required by a different BY team.
I : Action incomplete.
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CONCLUSION
The success or failure of a HAZOP study depends upon:
The accuracy of drawings & other documents used in the
study.
The expertise & experience of the team.
The ability of the team to visualize deviations, causes &consequences.
The ability of the team to assess the seriousness of
hazards.
The skill of the chairman in keeping the study on track.
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THANKS