Why Risk-Based Inspection (RBI) Works

The API Inspection Codes were originally based on failure prevention and did not consider the consequences of failure or potential damage mechanisms.  Risk-based inspection (RBI) assessments result in an equipment risk ranking based on the probability of failure (a leak occurring) and the consequence associated with that leak.  Applied properly, RBI provides the benefit of […]

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Risk Assessment of Refinery Hydroprocessing Unit Reactor Effluent Air Coolers (REACs) Made of Duplex Stainless Steel (DSS)

Cracking of REAC Duplex Stainless Steel Failures of Refinery Hydroprocessing Unit REACs made of 2205 DSS have in some cases resulted in significant plant damage and extended outages for repairs.  In a few  cases, header box welds have ruptured.  Additionally, failures have occurred at tube-to-tubesheet welds and in REAC inlet and outlet piping made of […]

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Are Your Heaters Affecting Your Reliability?

From a process standpoint, your Fired Equipment items are not only some of the most critical but some of the most risky items in day-to-day operations. Add in the presence of open flames and failures can be dramatic.  In today’s refining climate, fired equipment is required to run 4, 5, 6 or even 7 years […]

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CalOSHA Update – Damage Mechanism Reviews (DMR)

On May 18, 2017, the California Department of Industrial Relations’ Occupational Safety and Health Standards (CalOSHA) board approved a new regulation that changes how Process Safety Management (PSM) is handled for oil refineries within the state of California.  This regulation was approved in response to high-profile industry incidents in the state of California in the […]

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Reduced Toughness Properties of Some Modern Carbon Steels Create Brittle Fracture Risk

Changes in steelmaking practice are reported to be causing some carbon steel piping components that are assumed by ASME Codes to behave in a ductile manner at ambient temperatures, to behave instead in a brittle manner.  Barry Messer from Fluor made a presentation on this subject at the Spring 2016 meeting of the ASME B31.3, […]

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Changing Your Crude Slate – Short and Long Term Consequences

There are many reasons why a refinery may want to change their crude slates. However, all of them boil down to economics. Whether a cheaper crude is available or there is a desire to manufacture specific products to increase profitability – money is the driver. However, in deciding to change your crude slate, the long […]

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New Method for Prioritizing Equipment for Inspection and Replacement in HTHA Service

Gerrit Buchheim, Manager of the Pono Division of Becht Engineering, has developed a practical and simple-to-use approach to prioritizing the inspection and replacement of equipment in High Temperature Hydrogen Attack (HTHA) service.  This approach utilizes the existing and accepted “Nelson Curve”, but adapts it to better fit the realized operating conditions at an individual facility, […]

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Statistical Analysis of Non-Destructive Examination Data

In 2008, Becht Engineering was awarded a project by the Materials Technology Institute (MTI) to develop an inspection guideline document and software tool for the collection and analysis of inspection data for piping, piping components and pressure vessels. Dr. Eileen Chant , as project manager, collaborated with Bob Sims of Becht, Dr. Mark Stone of […]

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Materials Technology Institute Polymeric Risk-Based Inspection Pilot Project

Becht was selected by the Materials Technology Institute (MTI) to adapt its Risk-Based Inspection (RBI) methodology to develop an RBI work process for above-ground, fiberglass reinforced polymer (FRP) storage tanks.  The Becht RBI methodology, which complies with API RP 580, was initially used for metallic fixed equipment and has been expanded to other types of […]

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Computational Fluid Dynamics (CFD) Confirms Cause of Deaerator Cracking

CFD was used to confirm that poor design of the steam inlet nozzle was the main contributor to deaerator head to shell weld cracking, and confirmed proposed design improvements.  This recent Becht project illustrates one of the causes of deaerator cracking. A through-wall crack had been found at the head-to-shell junction at the steam inlet […]

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