Identifying and Understanding the Risk of Acoustic-Induced Vibration Failures

  • Home
  • Identifying and Understanding the Risk of Acoustic-Induced Vibration Failures

Identifying and Understanding the Risk of Acoustic-Induced Vibration Failures

Authors: Nathan D. Libertowski, Engineer II; Michael F.P. Bifano, Ph.D., P.E., Consulting Engineer I

Note: The following article was published in the March/April 2021 issue of the Inspectioneering Journal. Please submit the form below to access the full article. 

One source suggests that 10-15% of piping failures are a result of fatigue from vibration. Piping vibration can be caused by multiple different mechanisms such as flow-induced turbulence, slug flow, mechanical excitation from machinery, and acoustic pulsation. These mechanisms are often observed by plant operators since they present themselves during normal operation. On the other hand, acoustic-induced vibration (AIV) in pressure relief lines and downstream of control valves used for blow-down (BDV) is difficult to identify since the vibration is not readily observable unless the valves are opened. 

Often downstream of a pressure-reducing device (PRD), AIV occurs in gas systems when acoustic waves generated at flow restrictions excite natural modes of the piping, thus leading to vibration. AIV is different from most types of piping vibration because it generally occurs at much higher frequencies (300-1,500 Hz) and is the result of shell mode excitation. For this reason, AIV is typically not visible to the human eye but is noticeable by touch and transmits high-frequency audible noise outside the piping to the surrounding areas. The occasionality, combined with the high-frequency, low-amplitude vibration, allows AIV to usually go unnoticed until the vibration is heard, the pipe is touched, or a failure occurs. 

To continue reading the article, submit the form below:

Newsletter Archive

Access all of our previously published Industry Insights Newsletter articles:

Recently Published

Vessel Overpressure Protection Using System Design – No Relief Valve?  You’re Kidding, Right?

Author: Phil Henry, P.E., Process Technology Team Leader, Principal Engineer II

Even though PRDs are the industry standard for overpressure protection, there are cases when an instrumented system design approach can be a good alternative, if it meets ASME Section XIII, Part 13 requirements. Within this article, Phil Henry outlines key considerations, from assessing feasibility to ensuring compliance, and the key questions all owner-users should be asking.

Read More »

Analysis of Piping Surge Events

Authors: Bob Davis, P.E., Consulting Engineer II; Curtis Koether, P.E., Senior Engineer II

Surge events in piping systems can lead to severe displacements, loud noises, and operational challenges. Using a case study, this article highlights the factors behind surge events, including rapid changes in liquid velocity and pressure, and how forces generated during these transient events can impact piping systems. The authors discuss how a few targeted support modifications effectively resolved these issues without resorting to costly system overhauls or potentially problematic specialty equipment.

Read More »

Addressing Piping Vibration in the Oil, Gas, and Petrochemical Industries: The Upcoming API 579 Part 15

Author: Michael F.P. Bifano, Ph.D., P.E., ISO VCAT-IV, Rotating Equipment, Vibration, & Dynamics Team Leader

With the recent API Fall Meeting, it is timely to revisit this November 2023 article on API 579 Part 15, Methodologies of Piping Vibration, featuring insights from one of the new standard’s co-authors, Mike Bifano. This article discusses the three-tiered evaluation system and explains how vibration fits into a mechanical integrity program. Read more and learn about the highly anticipated improvements to our industry standards.

Read More »
Generic selectors
Exact matches only
Search in title
Search in content
Post Type Selectors
Pages
Industry Insights Newsletter Articles
Events
Library Items