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HAZOP
(Hazard Operability)
HAZOP Objective
 A hazard and operability study (or HAZOP) is a systematic,
critical examination by a team of the engineering and
operating intentions of a process to assess the hazard potential
of mal-operation or mal-function of individual items of
equipment and the consequential effects on the facility as a
whole.
 The HAZOP technique was initially developed to analyze
chemical process systems, but has later been extended to other
types of systems and also to complex operations and to
software systems.
Origin of HAZOP Study
 HAZOP were initially 'invented' by ICI in the United Kingdom, 1963
 HAZOP started to be more widely used within the chemical process
industry after the Flixborough disaster (UK) in 1974 that killed 28
people and injured scores of others.
 The system was then adopted by the petroleum industry, which has a
similar potential for major disasters.
 This was then followed by the food and water industries, where the
hazard potential is as great, but of a different nature, the concerns
being more to do with contamination rather than explosions or
chemical releases.
 International Standard IEC61882 (HAZOP Studies Application Guide
2001
When to perform a HAZOP ?
 HAZOP studies may also be used more extensively,
including: At the initial concept stage when Design
Drawings are available.
 When the final Piping And Instrumentation
Diagrams (P&ID) are available.
 During construction and installation to ensure that
recommendations are implemented.
 During commissioning.
 During operation to ensure that plant emergency and
operating procedures are regularly reviewed and
updated as required.
Types of HAZOP
 Process HAZOP
The HAZOP technique was originally developed to
assess plants and process systems
 Human HAZOP
A “family” of specialized HAZOPs. More focused on
human errors than technical failures
 Procedure HAZOP
Review of procedures or operational sequences
 Software HAZOP
Identification of possible errors in the development
of software
Prerequisites for HAZOP
As a basis for the HAZOP study the following information should
be available:
 Process flow diagrams
 Piping and instrumentation diagrams (P&IDs)
 Layout diagrams
 Material safety data sheets
 Provisional operating instructions
 Heat and material balances
 Equipment data sheets Start-up and emergency shut-down
procedures
HAZOP Procedure
 Divide the system into sections (i.e., reactor, storage)
 Choose a study node (i.e., line, vessel, pump, operating
instruction)
 Describe the design intent
 Select a process parameter
 Apply a guide-word
 Determine cause(s)
 Evaluate consequences/problems
 Recommend action: What? When? Who?
 Record information
 Repeat procedure (from step 2)
HAZOP TERMINOLOGIES
 Parameter
The relevant parameter for the condition(s) of the process
(e.g. pressure, temperature, composition).
 Deviation
A deviation is a way in which the process conditions may
depart from their design/process intent.
 Node
A node is a specific location in the process in which (the
deviations of) the design/process intent are evaluated.
Examples might be: separators, heat exchangers,
scrubbers, pumps, compressors, and interconnecting
pipes with equipment.
 Design Intent
The design intent is a description of how the process is
expected to behave at the node; this is qualitatively
described as an activity (e.g., feed, reaction,
sedimentation) and/or quantitatively in the process
parameters, like temperature, flow rate, pressure,
composition, etc.
 Guideword
A short word to create the imagination of a deviation of
the design/process intent. The most commonly used set
of guide-words is: no, more, less, as well as, part of, other
than, and reverse.
Guide-word + Parameter
Deviation
A scenario…
Someone on a road trip by using a car in the middle of the
night. A boy replying a text message while driving at 100
km/h and it was raining heavily. The car hits a deep hole
and one of your tire blows. He hit the brake, but due to
slippery road and his car tire thread was thin, the car
skidded and was thrown off the road.
Points to ponder……
What is the cause of the accident?
What is the consequence of the event?
What can we do to prevent all those things to
happen in the first place?
Can we make it more
systematic?
Parameter Guideword Possible
Causes
Consequences Action Safeguard
Car speed Too fast Rushing Skidded when
emergency
brake
- Slow down -ABS brake
system
-Safety belt
- Air bag
Tire No thread
Less thread
Tire too old,
often
speeding
and
emergency
break
Car skidded Change tire - Check
frequently
- Have spare
tire
Window
visibility
Low
Very low
Rain Cannot see the
road
T
C
Cooling Coils
Monomer
Feed
Cooling Water to Sewer
Cooling
Water In
Thermocouple
The reaction is exothermic. A cooling
system is provided to remove the
excess energy of reaction. In the event
of cooling function is lost, the
temperature of reactor would
increase. This would lead to an
increase in reaction rate leading to
additional energy release.
The result could be a runaway
reaction with pressures exceeding the
bursting pressure of the reactor. The
temperature within the reactor is
measured and is used to control the
cooling water flow rate by a valve.
Perform HAZOP Study
HAZOP Study (Flash Drum)

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hazop study.pptx

  • 2. HAZOP Objective  A hazard and operability study (or HAZOP) is a systematic, critical examination by a team of the engineering and operating intentions of a process to assess the hazard potential of mal-operation or mal-function of individual items of equipment and the consequential effects on the facility as a whole.  The HAZOP technique was initially developed to analyze chemical process systems, but has later been extended to other types of systems and also to complex operations and to software systems.
  • 3. Origin of HAZOP Study  HAZOP were initially 'invented' by ICI in the United Kingdom, 1963  HAZOP started to be more widely used within the chemical process industry after the Flixborough disaster (UK) in 1974 that killed 28 people and injured scores of others.  The system was then adopted by the petroleum industry, which has a similar potential for major disasters.  This was then followed by the food and water industries, where the hazard potential is as great, but of a different nature, the concerns being more to do with contamination rather than explosions or chemical releases.  International Standard IEC61882 (HAZOP Studies Application Guide 2001
  • 4. When to perform a HAZOP ?  HAZOP studies may also be used more extensively, including: At the initial concept stage when Design Drawings are available.  When the final Piping And Instrumentation Diagrams (P&ID) are available.  During construction and installation to ensure that recommendations are implemented.  During commissioning.  During operation to ensure that plant emergency and operating procedures are regularly reviewed and updated as required.
  • 5. Types of HAZOP  Process HAZOP The HAZOP technique was originally developed to assess plants and process systems  Human HAZOP A “family” of specialized HAZOPs. More focused on human errors than technical failures  Procedure HAZOP Review of procedures or operational sequences  Software HAZOP Identification of possible errors in the development of software
  • 6. Prerequisites for HAZOP As a basis for the HAZOP study the following information should be available:  Process flow diagrams  Piping and instrumentation diagrams (P&IDs)  Layout diagrams  Material safety data sheets  Provisional operating instructions  Heat and material balances  Equipment data sheets Start-up and emergency shut-down procedures
  • 7. HAZOP Procedure  Divide the system into sections (i.e., reactor, storage)  Choose a study node (i.e., line, vessel, pump, operating instruction)  Describe the design intent  Select a process parameter  Apply a guide-word  Determine cause(s)  Evaluate consequences/problems  Recommend action: What? When? Who?  Record information  Repeat procedure (from step 2)
  • 8. HAZOP TERMINOLOGIES  Parameter The relevant parameter for the condition(s) of the process (e.g. pressure, temperature, composition).  Deviation A deviation is a way in which the process conditions may depart from their design/process intent.  Node A node is a specific location in the process in which (the deviations of) the design/process intent are evaluated. Examples might be: separators, heat exchangers, scrubbers, pumps, compressors, and interconnecting pipes with equipment.
  • 9.  Design Intent The design intent is a description of how the process is expected to behave at the node; this is qualitatively described as an activity (e.g., feed, reaction, sedimentation) and/or quantitatively in the process parameters, like temperature, flow rate, pressure, composition, etc.  Guideword A short word to create the imagination of a deviation of the design/process intent. The most commonly used set of guide-words is: no, more, less, as well as, part of, other than, and reverse. Guide-word + Parameter Deviation
  • 10.
  • 11.
  • 12.
  • 13. A scenario… Someone on a road trip by using a car in the middle of the night. A boy replying a text message while driving at 100 km/h and it was raining heavily. The car hits a deep hole and one of your tire blows. He hit the brake, but due to slippery road and his car tire thread was thin, the car skidded and was thrown off the road.
  • 14. Points to ponder…… What is the cause of the accident? What is the consequence of the event? What can we do to prevent all those things to happen in the first place?
  • 15. Can we make it more systematic? Parameter Guideword Possible Causes Consequences Action Safeguard Car speed Too fast Rushing Skidded when emergency brake - Slow down -ABS brake system -Safety belt - Air bag Tire No thread Less thread Tire too old, often speeding and emergency break Car skidded Change tire - Check frequently - Have spare tire Window visibility Low Very low Rain Cannot see the road
  • 16. T C Cooling Coils Monomer Feed Cooling Water to Sewer Cooling Water In Thermocouple The reaction is exothermic. A cooling system is provided to remove the excess energy of reaction. In the event of cooling function is lost, the temperature of reactor would increase. This would lead to an increase in reaction rate leading to additional energy release. The result could be a runaway reaction with pressures exceeding the bursting pressure of the reactor. The temperature within the reactor is measured and is used to control the cooling water flow rate by a valve. Perform HAZOP Study
  • 17.