SIL and functional safety in rotating equipment
Unravelling the terminology and meaning of safety integrity level and functional safety in rotating equipment
Viewed : 5438
SIL (safety integrity level) is a very important safety indicator that has been extensively discussed, described and often misunderstood within the industry over the past years. The purpose of this article is to provide operators, reliability engineers, instrumentation engineers and department managers with a practical overview of the areas where SIL and functional safety are important in their daily business life. Note that, in the light of the International Electro-technical Commission (IEC) and most other safety relevant standards, risk is strictly defined as “harm to health safety environment” (HSE).
Potential economic losses resulting from process downtime are often one of the justifications for the realisation of process improvements. However, there are concerns in the industry that the implementation of additional and SIL certified machinery protection may add to the nuisance trip rate. This is discussed at the end of this article.
Most safety responsible staff members have gone through a HAZOP (hazard and operability study), evaluating imposed process weaknesses, potential risks and even working out ways to improve process safety. This very systematic approach has brought huge improvements to process industry safety and is still one of the key tools. It involves going through a process, step by step, looking left and right at what can go wrong under certain, even rare, circumstances. However, accidents are not entirely avoidable and in all cases some kind of risk remains and severe accidents still do happen. This is where IEC 61511, initially released in 1998, steps in with yet another systematic evaluation based on those imposed risks found out through the HAZOP.
IEC 61511 offers guidance to the process equipment operator, defining the SIL requirements necessary to be met by the machinery protection system of choice (also often called a safety instrumented system, or SIS, see Figure 1). It is important to note that the end user/operator is finally responsible for this evaluation as well as for the reduction of the remaining process risks to an acceptable damage level (HSE related). IEC 61511 requirements are mandatory and to be followed by operators. In the US, ANSI/ISA84.00.01-2004 was issued in September 2004 and it primarily mirrors IEC 61511. The European standards body CENELEC has adopted the standard as EN 61511 (see Figure 2).
LOPA, risk graph and risk assessments
Commonly, detailed risk assessments applying IEC 61511 criteria on the process hazard analysis (PHA) results are performed by expert consulting companies. An often seen approach is called layers of protection analysis (LOPA) assessment. The SIL of a SIS is derived by taking into account the required risk reduction to be provided by that function. IEC 61511 notes that this is best accomplished as part of a process hazards and risk analysis (PHA) to benefit from possible synergies and the information developed. Another way to obtain an overview of the appropriate SIL is the risk graph (see Figure 3). By following the path characterised through the four different risk parameters (occurrence probability, extent of damage, exposure time and hazard avoidance [once damage occurs]) the appropriate SIL1 to SIL4 will result (with 4 being the highest, most stringent SIL). The example within the risk graph indicates that even under rather dramatic circumstances (unexpected death of one person) a SIL1 machinery protection system would meet the IEC 61511 requirements in this respect.
The author wants to be very clear that the SIS is employed to prevent a severe HSE event and that severe harm or even the death of a person are not acceptable in any way. Every effort and technical advancement should be employed to prevent harm and HSE in general.
If a SIS is chosen to reduce the imposed process risks to the acceptable level it must meet the SIL requirement just evaluated.
IEC 61508, PFD and PTI
Vendors of SIS have to follow the guidance given under IEC 61508 when developing, testing and having them SIL certified. Stringent availability criteria must be met by each individual component employed inside a SIS. Also every single embedded algorithm is tested, improved if needed and finally approved by a certifying body such as TÜV or Exida with the appropriate SIL certificate. During the certification process as well as during the implementation phase, the probability of failure on demand (PFD) is one of the guiding values (see Figure 4). This is calculated by adding up the PFD for all individual components within each loop (demand = dangerous event occurs and component should perform as it is supposed to).
One very important factor with a linear impact on the PFD calculation is the proof test interval (PTI). The shorter the chosen PTI, the lower the PFD. Modern machinery protection systems offer the convenience of a two to three year PTI along with a SIL2 certificate, reducing the testing and documentation effort to an acceptable level.
Figure 4 shows the correlation of SIL and PFD values to be met per loop to meet the requirements. In order to meet SIL2, a PFD value of 10-2–10-3 (per hour; low demand mode) is required. The inverted value results in a theoretical systems availability of 99-99.90%.
It is important to note that the PFD evaluation must be done per each individual safety relevant loop, and must include all elements involved, from the sensing element down to the acting relay finally stopping the process/machine at acute risk, potentially resulting in HSE harm. It is not sufficient for one individual sensor, card or relay to be SIL certified and meet the appropriate PFD criteria – the entire loop must meet the PFD hence SIL requirement. Which sensors and characteristic sensors should be incorporated into a safety strategy depends heavily on the application and type of process equipment.
Boundary conditions when installing and planning a protection system
The two biggest fears related to machinery protection systems covering critical machinery are false trips, resulting in economic losses and sometimes dangerous process situations, and missed detects, which are simply dangerous.
On many safety critical applications it is mandatory to use sensor redundancy and voting logic to ensure proper system function and availability even when a single end device has failed and can often not be replaced while the process is operational.
There are different strategies available today to reduce the nuisance trip level of modern SIS to almost zero, while in parallel ensuring severe events are detected timely and the machinery is safely shut down with minimum consequential damage.
Sensor redundancy and voting
One frequently chosen strategy is the application of sensor redundancy. Voting schemes include 1-out-of-n voting, n-out-of-n voting and n-out-of-m voting (2oo3 or 2oo4). The n-out-of-m voting involves a higher number of sensors being installed, but offers a feasible way of reducing both spurious and missed trip rates.
Alternatively, modern systems also offer an interesting alternative using diagnostic coverage (DC) in a 1oo1D sensor architecture, employing a single sensor per location and closely monitoring its proper function at all times (DC>99%) and thereby achieving a higher SIL.
Add your rating:
Current Rating: 4