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A hazards analysis technique specifically structured to analyze
equipment items is Failure Modes & Effects Analysis (FMEA). The
method examines the ways in which an equipment item can fail (its
failure modes), and examines the effects or consequences
of such failures (safety, reliability or environmental performance).
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If the criticality of each failure is to be considered,
then the method becomes a Failure Modes, Effects and Criticality (FMECA)
Analysis.
Methodology
The following process for conducting an FMEA is adapted
from the American Society for Quality system.
- Assemble a cross-functional team (how this can be done is discussed
at the page
HAZOP Team Selection and Management). The team should represent
designers, operations, maintenance and the end user.
- Define the physical scope of the FMEA. For example, in the heat
exchanger analysis discussed below, determine if utility systems such
as the cooling water supply are to be included.
- Define the purpose of the equipment item being examined.
- Identify the failure modes for that equipment item and determine
their consequences and their likelihood.
- Determine if the analysis is to incorporate the effect of
safeguards and controls.
Team Process
Like other types of hazards analysis, an FMEA should
be carried out by a team. In most cases, however, only two or three team
members - who are specialists in the required fields - are involved. The
FMEA scribe will complete a form such as that shown below which is written
for the heat exchanger shown in Figure 2 in the
Examples Page.
FMEA Analysis of Heat Exchanger
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#
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Failure Mode
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Cause(s)
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Indications/ "Announce-ment"
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Predicted Frequency
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Consequences
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Risk
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1
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Tube failure
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Corrosion from fluids (shell side).
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Odors at the cooling tower.
Hydrocarbon detector on the tower.
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Frequent - has happened twice in ten years.
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Hydrocarbon is at higher pressure than the cooling water.
Therefore flammable materials could enter the cooling tower
and cause a major fire.
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2
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Tubesheet failure
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See tube failure. Vibration of the
tubes may cause the sheet to fail even if the tubes hold
up.
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See #1.
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Rare
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See #1.
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3
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Relief valve fails open
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1. Mechanical failure
2. External impact
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Hydrocarbons to atmosphere - fire and environmental hazard
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Rare
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Serious
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4
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Relief valve fails closed
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1. Mechanical failure
2. Polymer buildup
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None (passive failure)
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Uncommon
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Critical
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5
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Erosion of tubes
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High velocity of cooling water
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See tube failure
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Rare
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Critical - see tube failure
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6
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Vent valve fails open
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Mechanical failure
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See relief valve fails open
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Rare
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Serious
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7
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Vent valve fails closed
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Mechanical failure
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None (passive failure)
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Rare
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Minor - could lead to problems for turnaround maintenance
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8
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Drain valve fails open
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Mechanical failure
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See "relief valve fails open".
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Rare
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Serious
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9
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Drain valve fails closed
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See vent valve fails closed.
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10
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Corrosion (tube side)
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Incorrect process composition.
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See tube failure
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Uncommon
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Critical
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The Table has seven columns. The purpose of each is discussed below.
- The first column is the number of the failure mode for that item
of equipment.
- The second column identifies the failure mode.
- The third column lists possible causes of the failure mode. Although
identification of causes is not a requirement of the FMEA process, they
do need to be identified so that appropriate corrective actions can
be taken.
- Column four lists the signs by which operations personnel know that
the event has happened.
- The fifth column provides an estimate for the number of times the
failure mode is likely to happen.
- The sixth column identifies the potential consequences of the failure
mode. As already noted, the consequences will vary depending on the
magnitude of the failure. The consequence that is usually of most interest
is injury of personnel. However, environmental impact and economic loss
can also be considered. Some practitioners have two levels of consequence:
immediate and 'end effect'. In the first row, the immediate effect of
a tube failure is hydrocarbons in the cooling tower; the ultimate effect
could be a catastrophic fire in the cooling tower.
- The last column provides an estimate for the level of risk associated
with the failure mode.
Severity
The list below provides a means of estimating the severity
of the event.
- None. No effects observed.
- Minor. System operable with some loss of efficiency or quality.
- Low. System operation will cause some equipment damage but
should not create a safety hazard.
- Moderate. System operation will cause equipment damage and
could create a safety hazard.
- High. System operation will cause significant equipment damage
and is likely to jeopardize safety.
- Very High. System operation will lead to destructive failure
with a significant chance of someone being hurt and/or the creation
of a major environmental problem.
In all cases, the severity of the event will depend on whether it occurs
with our without warning, with the second of the two obviously being the
more serious.
The FMEA method is one of the techniques used in
Process Hazards Analyses (PHAs) to identify and risk rank hazards. The OSHA
regulation lists the following allowable techniques:
Process Hazards Analysis
The FMEA method is one of the techniques used in
Process Hazards Analyses (PHAs) to identify and risk rank hazards. The OSHA
regulation lists the following allowable techniques:
- What-If;
- Checklist;
- What-If / Checklist;
- Hazard and Operability Study (HAZOP)
- Failure Modes and Effects Analysis (FMEA);
- Fault Tree Analysis; or
- An appropriate equivalent methodology.
Since the focus of a Process Hazards Analysis is
on the identification of process or system-related issues, an FMEA would
generally serve to support one of the other techniques, such as HAZOP. For
example, a HAZOP may consider the system effects of a heat exchanger failure;
the FMEA, as shown above, would then examine the exchanger itself in more
detail.
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