It’s easier to express probability in
terms of failure, rather than in terms of
proper performance. As published in the
aforementioned standards and some
product brochures, four levels of SIL
are listed, enumerated 1-4—the higher
the SIL level, the higher the associated
safety level, and the lower probability
that a system will fail to perform properly (Figure 1).
These various SIL levels might be
correlated to the above mentioned
examples of consequences of failure.
For purposes of this article, it is
appropriate to think of SIL as “the
degree of likelihood that our system will
work when we want it to.” (Generally,
SIL 4 is beyond the scope of what we
see in the process industries.) Again, we
might want to think of a “function” as
an emergency shutdown valve system,
typically consisting of a sensor of some
type (pressure, level, temperature) and a
logic controller that will send a signal to
an automated valve. The automated
Detail
0.1
0.01
0.001
Time
Partial Test
Partial Test
Full Test
Full Test
Figure 3. PFDAVG is decreased due to PST combined with full cycle testing
valve package might consist of an
actuator (pneumatic, electric, hydraulic,
etc.), solenoid valves, quick exhaust
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valves and the final control element, the
valve. The “system” may consist of
many functions; it might have five emergency shutdown valves protecting a
pressure vessel cooking a process. Or, it
might have only one function (the SIF)
making the entire SIS.
To summarize, the HAZOP team will
determine SIL levels based on determined PFD. Michael Young of General
Monitors has summed this issue up nicely in his paper, SIL 101: How Safe Do I
Need to Be?
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A simple example will help illustrate the concepts of SIS, SIF, and SIL.
Consider the installation of a pressure
vessel containing flammable liquid. It
is maintained at a design operating
pressure by the Basic Process Control
System (BPCS). If the process control
system fails, the vessel will be subjected to an over-pressure condition
that could result in a vessel failure,
release of the flammable contents
and even fire or explosion. If the risk
in this scenario is deemed to be
intolerable by the facility owner,
an SIS will be implemented to
further reduce this risk situation to
a tolerable risk level.
The SIS system will be independent
from the BPCS and will act to prevent