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Plantilla de excel para aplicar la metodología HazopDescripción completa
Sample of a HAZOPFull description
Hazard & Operability Assessment (HAZOP) Process Unit: Ammonia Separation and Storage P&ID No. Section/Node:
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Study Date: Property Pressure
Process Parameters: Pressure Guide Word No More of Less of Part of
Deviations No Pressure More Pressure Less pressure
Consequences
Causes
Suggested Controls
Causes
Suggested Controls
Causes
Suggested Controls
Process Parameters: Temperature Property Temperature
Guide Word No More of Less of Part of
Deviations
Consequences
Process Parameters: Flow Property Flow
Guide Word No More of Less of Part of
Deviations No Flow
Consequences
1
Process Parameters: Level Property Level
Guide Word No More of Less of Part of
Deviations
Consequences
Causes
Suggested Controls
Causes
Suggested Controls
Process Parameters: Concentration Property Concentration
Guide Word No More of Less of Part of
Deviations
Consequences
Team members:
2
Scope of work
The HAZOP study will be carried out on area 5. The HAZOP study should consider the following: 1. Initial start-up 2. Normal operation 3. Maintenance shut down 4. Emergency shut down 5. Start up after shut downs
Evaluating causes and consequences (Chevron) Causes Brainstorm all possible causes related to human factors and equipment performance Don’t analyse during brainstorming Stay within section during brainstorming ( Special note: feed nodes from off-plots, it is acceptable to identify causes from the node) Don’t criticize during brainstorming Discuss all realistic causes in detail
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Develop Consequences Without Safeguards Check that all consequences take system out of design envelope, i.e. outside the intended range of operation Must identify ALL consequences (immediate and delayed both inside and outside section of analysis, injury, fire, damage, environmental or economic impact), eg compressor failure will result in shutdown of plant will eventually result in total facility shutdown Note how consequences develop, ie how how deviation will trigger alarms/ trips, etc, to trigger operator intervention Considerations: Operator is not available or is not paying attention Control valve are in manual Alarm and safety interlocks do not function Procedures are not followed or are not understood
Part of “ only some of the design intention achieved”