Risk based inspection (RBI) is a powerful tool to identify and manage mechanical integrity risks in fixed equipment and piping but is only one part of a robust reliability program. RBI informs inspection decision making on where, when and how to inspect most of equipment but is frequently misinterpreted as a “Silver Bullet” that covers all necessary inspection activities in a refinery. Most RBI programs have significant gaps that can result in costly reliability issues or unjustified maintenance costs.
RBI gaps can exist where risk assessments require input from outside of an inspection department or mechanical integrity group. Examples of these gaps are when failures have process consequences but not mechanical integrity concerns, such as tube leaks in shell and tube heat exchangers and cyclones in an FCC Unit. Another example is when mechanical integrity is dependent upon other systems functioning per design, such as fired heater tubes. Quantitative RBI Programs are not equipped to capture these types of failure scenario or risks. API-581 does Includes a methodology for calculating tube bundle life, but this module provides only one piece of puzzle to risk assess tube failures.
We can examine a Crude Unit feed preheat exchanger as an example. The atmospheric tower feed is preheated in a shell and tube heat exchanger using the tower bottoms reflux as the heating medium. The feed is at a higher operating pressure than the reflux so in the event of a tube leak, desalted crude will leak into the reflux which is sent back into the atmospheric tower. The consequence of a small leak is minimal and is unlikely to be detected. As the leak increases in size and is eventually detected, a planned outage can be taken for repairs. This is an example of a low consequence tube leak.
We can contrast the feed preheat exchanger scenario with a higher consequence tube leak on a product rundown exchanger. The purpose of the rundown exchanger is to cool finished products enough to meet tankage temperature limits. The finished product must meet specifications and even a small leak can result in off-spec product. A leak will be detected during sampling and the exchanger will have to be isolated for repair immediately or risk a tank full of off-spec product. Depending on the configuration of the unit, this leak can result in lost production and a financial consequence that is not normally captured as part of an RBI Program.
From a reliability perspective, the consequences of tube leaks for these two exchangers differ significantly. Therefore, the inspection technique, inspection frequency, and bundle replacement strategy should differ as well. To develop a comprehensive strategy requires process, operations, and inspection working together to develop a holistic reliability plan.
Part of the solution can be to develop a criticality ranking for tube bundles. Rankings can be separated into three categories (high, medium, and low) depending on the consequences of tube leaks. The main considerations in the criticality ranking are as follows:
The bundle criticality can then be paired with the probability of failure and used to determine level of inspection, and tube retirement criteria.
Another example of a typical gap in an RBI program is fired heaters, which exemplify a multi-disciplinary type of equipment. Safe and reliable operation of fired heaters requires input from inspection, operations, process, instrumentation, and fireside and refractory specialists at various times in the equipment lifecycle.
Fired heater tubes are commonly treated as a piping circuit or pressure vessel in RBI programs which can lead to poor reliability and unexpected failures. Mechanical integrity of heater tubes is dependent upon reliable operation of heater systems including burners and instrumentation. Tubes also require different types of surveillance than a regular piping circuit or pressure vessel.
For example; in hydro-processing units at the beginning of a turnaround cycle the fired heaters run at lower temperature because the catalyst in reactors is fresh and very active. Over the run, the catalyst activity decreases and this is compensated for by increasing the firing rates of the heaters. These increased firing rates can exceed tube metal temp (TMT) limits, potentially resulting in creep damage, carburization and reduced tube life.
High TMTs can also be caused by several things including temperature excursions, burner fouling or damage, over firing, scale build-up, or internal fouling. Managing the mechanical integrity of fired heater tubes requires more than just inspection. It requires setting and stewarding TMT Limits, operational awareness of limits, notification of inspection as conditions change, and inspection planning that corresponds with unit operational cycles.
The first step is awareness and identification of the gaps in your RBI Program. Then, tools and work processes need to be identified to address your specific gaps. Here are some examples of work processes that can be used to fill the gaps:
For information on Becht Services that can help address Gaps in RBI Programs follow the links below:
Reliability of Fired Heaters OR Equipment Reliability Planning
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Abby King has over 10 years of mechanical engineering experience in the Oil & Gas Industry. Mr. King’s areas of expertise include FCCU maintenance and turnarounds, pressure vessel design, and risk based reliability work. He has built turnaround work scopes and packages utilizing risk based work selection and developed equipment strategies for existing and grass roots units. His turnaround engineering support includes unit coverage of FCC, HF Alkylation, Crude, Coker, Hydrotreating, Sulfur and Utilities units. His software experience includes use of Auto Cad 3D, PV Elite, Compress, Math Cad, VCESage 8.0 and Caesar II Software.
Abby holds a B.S. degree in Mechanical Engineering from Carnegie Mellon University, Pittsburgh, PA and is an API Certified 510 Pressure Vessel Inspector.
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