Safety and environmental standards for fuel storage sites
Final report
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35 Systems providing a risk reduction of less than 10 are not in scope of BS EN 61511. They
may, however, still provide a safety function and hence are safety systems and can be a layer of
protection. Such systems should comply with good practice in design and maintenance so far as
is reasonably practicable.
36 Shutdown of product flow to prevent an overfill should not depend solely upon systems or
operators at a remote location. The receiving site should have ultimate control of tank filling by
local systems and valves.
37 The normal fill level, high alarm level and high-high alarm/trip level should be set in compliance
with the guidance on designating tank capacities and operating levels.
38 Tank level instrumentation and information display systems should be of sufficient accuracy
and clarity to ensure safe planning and control of product transfer into tanks.
Application of LOPA to the overflow of an atmospheric tank
39 The dutyholders should review the risk assessment for their installations periodically and take into
account new knowledge concerning hazards and developments in standards. Any improvements
required by standards such as BS EN 61511 should be implemented so far as is reasonably
practicable.
40 LOPA is one of several methods of risk assessment that can be used to facilitate SIL
determination; BS EN 61511 Part 3 provides a summary of the method. Other methods described in
BS EN 61511, eg risk graphs, are equally acceptable for the determination of SIL. Detailed guidance
for the application of LOPA to the overflow of an atmospheric tank is provided in Appendix 2.
Incorporating the findings of SIL assessments into COMAH safety reports
41 The findings of the SIL assessment, using the common methodology, should be included in
the COMAH safety report for the site. This should provide sufficient detail to demonstrate that:
the overall systems for tank filling control are of high integrity, with sufficient independence to
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ensure timely and safe shutdown to prevent tank overflow; and
SIS and management systems should be commensurate with the requirements of
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BS EN 61511, so far as is reasonably practicable.
Operator responsibilities and human factors
42 Monitoring and control of levels, and protection against overfill, may depend on operators
taking the correct actions at a number of stages in the filling procedure. These actions may
include, but not be limited to:
calculation of spare capacity;
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correct valve line up;
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cross-checks of valve line up;
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manual dipping of tank to check automatic tank gauging (ATG) calibration;
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confirmation that the correct tank is receiving the transfer;
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monitoring level increase in the correct tank during filling;
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checks for no increase in level in static tanks;
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closing a valve at the end of a transfer;
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response to level alarm high (LAH); and
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response to level alarm high-high (LAHH).
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