Safe Operating Limits - API 754

Operational issues of any Petrochemical plant or Oil and gas field, upstream issues, etc.
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ivani1
Posts: 156
Joined: 25 May 2025, 14:25
Area of interest: Mechanical Engineering

Safe Operating Limits - API 754

Post by ivani1 »

What exactly safe operating limits reporting be based upon as per API 754? Design limit excursion itself, right?
And how that should be reviewed? Every time the limit exceeds, without any delays?
opo21
Posts: 73
Joined: 22 Dec 2025, 08:14
Area of interest: Chemical Engineering

Re: Safe Operating Limits - API 754

Post by opo21 »

Safe Operating Limits are not always identical to absolute engineering design limits (such as maximum allowable working pressure - MAWP or ultimate design temperatures). Instead, SOLs are operational boundaries established by the facility, often incorporating Integrity Operating Windows (IOWs), control limits, and process safety information, beyond which the plant should not intentionally be operated.
chem51
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Re: Safe Operating Limits - API 754

Post by chem51 »

In simple words, "SOLE-Max & SOLE-Min process values in the system is defined as HH/LL alarm value which is safe operating limit or SIS activation value."
"OWEL is the process value which will be measured between 50% of high/low alarm valve and of high-high/low-low alarm value ( SIS activation value)."
Reportable value is exceedance of SOLE as per API 754.
jeem
Posts: 132
Joined: 10 Aug 2025, 17:25
Area of interest: Chemical Engineering

Re: Safe Operating Limits - API 754

Post by jeem »

The central principle is that an SOL is a defined process safety boundary, not simply an alarm setpoint or the equipment's maximum design rating.
That has to be correctly defined, documented, approved and applied at plants.
Controlled procedures should be made available enabling the system to generate an exceedance on daily basis so that those can be reviewed and acted upon in time.
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