Structural Integrity Associates and C2C Technical Services Announce the Formation of SI Solutions in Partnership with Jumana Capital

CHARLOTTE, NC – Structural Integrity Associates (“SI”) www.structint.com, a leading specialty engineering consultant in the power and utility industry, and C2C Technical Services (“C2C”) www.c2ctechnicalservices.com, a leading electrical engineering and electrical field service company, are pleased to announce the formation of SI Solutions, LLC (“SI Solutions”) in partnership with Jumana Capital (“Jumana”) www.jumanacapital.com, a Houston, TX-based private investment firm specializing in partnerships with entrepreneur led companies.

SI was founded in 1983 in San Jose, CA, as an engineering and consulting firm dedicated to the analysis, control, and prevention of structural and mechanical failures with a core focus on critical equipment and structures in the power generation and utility infrastructure. Living true to the motto, “Powered by Talent and Technology,” SI has established itself as an innovative and responsive resource for answering any challenge ranging from R&D to engineering, metallurgy, fabrication, and non-destructive evaluation (NDE).

Texas City, TX-based C2C provides electrical engineering and specialty field services, including automation, instrumentation, electrical services, and technical staffing services for critical infrastructure maintenance within the renewables, petrochemical, and refining sectors.

SI Solutions will be a leading provider of mission-critical power and infrastructure engineering, testing, and maintenance services focused on existing assets.  The platform will have more than 500 employees and nine offices, serving customers across the U.S. and internationally.  The leadership team of SI Solutions will be comprised of the management teams of both SI and C2C, including C2C founders Charles Roachell and Craig Miller. Mark Marano, the former COO of the Westinghouse Electrical Company, came out of retirement to become the CEO of SI in February 2020 and will be the CEO of SI Solutions, in addition to remaining the CEO of SI. The CFO of SI Solutions will be Michelle Digilormo; Cam Tran will serve as Executive Director of HR.

“The SI Solutions platform with SI and C2C is the perfect fit for both companies.  The combination enhances both platforms’ ability to grow and better serve client needs through additional investments in research and development, technical capabilities, field service offerings, and geographic reach. I am very excited about the future of SI Solutions,” said Mark Marano, CEO of SI.

“We are proud of what we’ve built at C2C and are excited to continue to drive growth in this next chapter”, says Charles Roachell, founder and co-president of C2C, “we believe our partnership with SI creates a best-in-class engineering and specialty service platform, led by a culture of safety and best practices. We will deliver the highest quality services to our customers and employees. We are excited to take the next step in building our platform”.

“The cultural fit of SI and C2C is unmatched in the industry”, says Craig Miller, founder, and co-president of C2C. “We value our highly skilled employee base and believe the combination of SI and C2C will create excellent opportunities for our employees to continue their professional and personal development. SI Solutions has an extremely bright future that we’re thrilled to be a part of”.

Chris Martin, Chief Investment Officer and Managing Director of Jumana Capital remarked, “SI Solutions is extremely well positioned to help meet the growing needs for asset management, compliance, maintenance, repair, and upgrade within the power generation, utility infrastructure, chemical, refining, and critical structures sectors in the United States and abroad. We are building something extraordinary and are excited for what the future holds for SI Solutions”.

 

Media Contact
Chris Sydor
Manager of Marketing and Communications
Structural Integrity Associates, Inc
info@structint.com
704-977-1361

High Energy Piping (HEP) Seminar 2023

January 31ST – February 2ND 2023

COURSE DESCRIPTION

Our High Energy Piping (HEP) Seminar for the Power Industry will be held over 2.5 days (January 31st – until noon on February 2nd) in Austin, TX. During this time, we’ll share our comprehensive expertise on specific topics geared towards being proactive with regards to managing these assets. As the energy landscape has shifted and the call for more flexible operation has increased, it’s important that strategies are in place to ensure personnel safety and unit reliability are maintained. SI aims to provide attendees with a rich educational experience surrounding the following technology areas to provide a holistic review of component health:

THIS SEMINAR IS ESPECIALLY RELEVANT FOR

  • Plant Managers
  • System Engineers and Managers
  • Corporate Piping Engineers
  • Metallurgists
  • Engineering and Maintenance Managers
  • Anyone interested in gaining knowledge of high energy piping systems is welcome

INSTRUCTORS

  • Ben Ruchte – Director, Senior Metallurgist
  • Kane Riggenbach – Senior Consultant, Analytical Services
  • Steve Gressler – Technical Director/Account Executive

COURSE TOPICS

Development and Management of an HEP program

  • Elements of a program
  • Components and systems included
  • Code requirements
  • Best practices

Stress analyses (explanation of the intricacies, when, what, and how to apply)

  • Creep redistribution
  • Creep lifetime prediction
  • Creep crack growth
  • Fatigue: aspects of cycling (operational data needs)

Metallurgical analyses (lab tour of SI’s Materials Lab, which may include an interactive review of samples)

  • Piping damage mechanism
  • Industry issues
  • Grade 91 refresher/update

Application of NDE (new techniques, post-processing methods, when, what, and how to apply)

  • Code versus serviceability examinations
  • Post-processing methods
  • Spray-on transducers
  • Technique and component matching

Continuous monitoring and data management

  • Data to be managed
  • PlantTrack
  • Online monitoring damage tracking

EVENT DETAIL

Event Date
Tuesday, January 31st – Thursday, February 2nd

Duration
8:00am to 5:00pm Tues. and Wed. 8:00am to 12:00pm on Thurs.

Individual Price
$1,195

Location
Lone Star Court
10901 Domain Drive Austin, Texas 78758
Telephone: 512-814-2625

We have negotiated a rate of $199/night plus taxes, you must book before January 10th to receive group rate. For reservations call 855-596-3398 and mention “SI HEP Seminar” to receive the group rate. Or you can book online using our booking link HOTEL REGISTRATION.

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Structural Integrity Associates | News and Views, Volume 51 | Optical Microscopy | Applications and Benefits

News & Views, Volume 51 | Optical Microscopy Applications and Benefits

By:  Clark McDonald

In the world of metallurgical failure analysis, areas of interest on broken parts can be colorful or drab, three-dimensional or flat, and most importantly, very big or very small.  A big part of failure analysis work is telling the story, explaining the failure mode, or in some cases, showing that critical piece of evidence that explains why a metal component has failed.  From wide-angled lenses to extremely high magnification scanning electron microscope imagery, documentation of failed components is a big part of the presentation.  

In this edition of Structural Integrity’s Lab Corner, we wanted to provide some interesting content related to that middle-of-the-road region of magnification; closer than macro-photography but farther away than the 100X to 5000X magnifications that cover most of the applications requiring scanning electron microscopy.  In other words, the comfortable world of optical microscopy, where colors, shapes, and even surface textures are part of the story.  To do this, we’ve chosen some images that show the usefulness of quality optical microscopic documentation.  Each of the provided examples include a brief description along with specific comments on the benefits of optical microscopy for that project, where applicable.

Figure 1. Two- and three-dimensional color images of an aluminum annode plate showing light-colored deposits that have caused uneven wastage. The 3D image shows the extent of material removal in locations where deposits are not present. Normal wastage in this application should be uniform.

Figure 2. Two- and three-dimensional color images showing fastener thread flank damage and a crack origin near the root of the upper thread. The 3D image shows that the crack origin is located on the thread flank rather than at the deepest part of the thread root.

Figure 3. Two- and three-dimensional images of a copper heat exchanger tube that has been damaged from under-deposit corrosion (UDC). The image at left shows the typical appearance of the ID deposits. The center image shows a region of damage surrounding a pinhole leak. The 3D image provides an idea of the depth of internal corrosion in the tube.

Figure 4. Two- and three-dimensional images of a region of damage on an internal surface of a feedwater pump. The image at left shows the appearance of brownish deposits found within the corroded region of the pump surface. The 3D image provides an indication of the depth and shape of the corrosion damaged region.

Figure 5. Two dimensional stitched image of a weld cross section showing cracking emanating from a shallow weld root. Porosity is also visible in multiple locations in the weld.

Figure 6. Images of a region of damage on the exterior of a heat exchanger tube where wastage has occurred near the tube sheet. The upper right image is a view of the leak location with an overlay of lines showing the position where the surface profile was documented as well as the depth profile (overlaid and in the lower image). The upper left image, which has an appearance similar to an x-ray, is a side view of the 3D image of the tube surface.

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News & Views, Volume 51 | Drone Inspections

SI EXPANDED CAPABILITIES

By:  Jason Van Velsor and Robert Chambers

Structural Integrity (SI) has recently added drones to our toolbox of inspection equipment. Using drones, inspectors are able to complete visual inspections safely and more efficiently. Applications of drones for visual inspections include plant and piping walkdowns, structural inspections and atmospheric corrosion monitoring (ACM) of exposed pipeline.

Figure 1. Drone image of a dent on an elevated section of pipeline

Pipe hanger walkdowns at fossil and combined cycle plants are part of a routine inspection process. During these inspections, the inspector is required to view and mark down pipe hanger positions and assess their condition. While some hangers provide easy access for the inspector, this is not always the case. Some of these may be located in elevated positions that require the plant to build out scaffolding, which not only increases the cost, but also can put the inspector at risk when working at elevation. With the use of drones, the inspector can fly up to the pipe hangers from a safe location and get a live high-resolution video feed from the camera mounted on the drone. Saving pictures and the video footage can also allow the inspector to go back and review the footage at a later time.

ACM is another example where drones have proven to be a useful tool. ACM inspections of outdoor above ground pipelines are typically done by

walking down the pipeline and recording any signs of atmospheric corrosion. There are many occasions where the pipeline will be elevated or cross over rivers and railroads, requiring scaffolding or fall protection. By using a drone to fly along the pipeline, the inspection can be completed much more efficiently and safely. In situations where a GPS signal is available, such as outdoor pipeline inspections, the GPS coordinates can be saved with each photo. Custom SI-developed software can then automatically compile the acquired images and create a KML file to be viewed in Google Earth, allowing the client to get an overview of the inspection results. 

Figure 2. Google Earth view of image locations

Moving forward, SI plans to utilize these drones for more than just visual inspections. Possible applications could include using drones to perform ultrasonic thickness testing or Structural Integrity Pulsed Eddy Current (SIPEC™) examinations. All of SI’s pilots in command hold valid FAA Part 107 certificates and pilot registered drones.

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Structural Integrity Associates | News and Views, Volume 51 | Pitting Corrosion in Conventional Fossil Boilers and Combined Cycle:HRSGs

News & Views, Volume 51 | Materials Lab Featured Damage Mechanism

PITTING CORROSION IN CONVENTIONAL FOSSIL BOILERS AND COMBINED CYCLE/HRSGS

By:  Wendy Weiss

Pitting is a localized corrosion phenomenon in which a relatively small loss of metal can result in the catastrophic failure of a tube. Pitting can also be the precursor to other damage mechanisms, including corrosion fatigue and stress corrosion cracking. Pits often are small and may be filled with corrosion products or oxide, so that identification of the severity of pitting attack by visual examination can be difficult. 

Figure 1. Severe pitting in a tube from a package boiler

Mechanism 

Pitting is a localized corrosion attack involving dissolution of the tube metal surface in a small and well-defined area. Pitting corrosion can occur in any component in contact with water under stagnant oxygenated conditions. Pitting in economizer tubing is typically the result of poor shutdown practices that allow contact with highly-oxygenated, stagnant water. Pitting also may occur in waterwall tubing as a result of acidic attack stemming from an unsatisfactory chemical cleaning or acidic contamination. 

Pits that are associated with low pH conditions tend to be numerous and spaced fairly close together. The pits tend to be deep-walled compared to the length of the defect. A breakdown of the passive metal surface initiates the pitting process under stagnant oxygenated conditions. A large potential difference develops between the small area of the initiated active pit (anode) and the passive area around the pit (cathode). The pit will grow in the presence of a concentrated salt or acidic species. The metal ion salt (M+A-) combines with water and forms a metal hydroxide and a corresponding free acid (e.g., hydrochloric acid when chloride is present). Oxygen reduction at the cathode suppresses the corrosion around the edges of the pit, but inside the pit the rate of attack increases as the local environment within the pit becomes more acidic. In the event that the surfaces along the walls of the pit are not repassivated, the rate of pit growth will continue to increase since the reaction is no longer governed by the bulk fluid environment. Pitting is frequently encountered in stagnant conditions that allow the site initiation and concentration, allowing the attack to continue. 

The most common cause of pitting in steam touched tubing results from oxygen rich stagnant condensate formed during shutdown. Forced cooling and / or improper draining and venting of assemblies may result in the presence of excess moisture. The interface between the liquid and air is the area of highest susceptibility. Pitting can also be accelerated if conditions allow deposition of salts such as sodium sulfate that combine with moisture during shutdown. Volatile carryover is a function of drum pressure, while mechanical carryover can increase when operating with a high drum level or holes in the drum separators. Pitting due to the effects of sodium sulfate may occur in the reheater sections of conventional and HRSG units because the sulfate is less soluble and deposits on the internal surfaces. During shutdowns the moisture that forms then is more acidic. 

Figure 2. Pitting on the ID surface of a waterwall tube

Typical Locations

In conventional units, pitting occurs in areas where condensate can form and remain as liquid during shutdown if the assemblies are not properly vented, drained, or flushed out with air or inert gas. These areas include horizontal economizer tubes and at the bottom of pendant bends or at low points in sagging horizontal tubes in steam touched tubes. 

In HRSGs, damage occurs on surfaces of any component that is intentionally maintained wet during idle periods or is subject to either water retention due to incomplete draining or condensation during idle periods. 

Attack from improper chemical cleaning activities is typically intensified at weld heat affected zones or where deposits may have survived the cleaning. 

Features

Pits often are small in size and may be filled with corrosion products or oxide, so that identification of the severity of pitting attack by visual examination can be difficult. 

Damage to affected surfaces tends to be deep relative to pit width, such that the aspect ratio is a distinguishing feature. 

Root Causes

Figure 3. Pitting on the ID surface of an economizer tube

The primary factor that promotes pitting in boiler tubing is related to poor shutdown practices that allow the formation and persistence of stagnant, oxygenated water with no protective environment. Confirming the presence of stagnant water includes: 

  1. analysis of the corrosion products in and around the pit; 
  2. tube sampling in affected areas to determine the presence of localized corrosion; and 
  3. evaluation of shutdown procedures to verify that conditions promoting stagnant water exist. 

Carryover of sodium sulfate and deposition in the reheater may result in the formation of acidic solutions during unprotected shutdown and can result in pitting attack. Similarly flyash may be pulled into reheater tubing under vacuum and form an acidic environment.

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PWR Operational Chemistry Training

November 7th – November 11th 2022

COURSE DESCRIPTION

This course provides practical, hands-on information and techniques for personnel responsible for operational chemistry analysis, corrosion prevention, and system diagnostics. Attendees are encouraged to bring plant data for group discussion and analysis. Common topics will be covered as well as reactor coolant chemistry and radiochemistry, steam generator and balance of plant chemistry, demineralizer and filtration performance, start up and shutdown chemistry, corrosion concerns, and data evaluation techniques.

WHO SHOULD ATTEND

Chemists and Engineers who desire a practical knowledge of primary and secondary operational water chemistry. This core course is designed for chemistry personnel that have a basic understanding of plant operation and plant systems, focusing on the essentials of primary and secondary operational water chemistry.

EVENT DETAILS

Event Date
Monday, November 7th – Friday, November 11th, 2022

Duration
8:00 a.m. to 4:30 p.m. Friday 8:00 a.m. to 12:00 p.m.

Individual Price
$2,200 (Includes light breakfast and lunch) Includes PWR Operational Chemistry Handbooks

Location
Constellation Cantera Corporate Office
4300 Winfield Rd, Warrenville, IL 60555

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BWR Operational Chemistry Training

October 31st – November 4th 2022

COURSE DESCRIPTION

This course provides practical, hands-on information and techniques for personnel responsible for operational chemistry analysis, corrosion prevention, and system diagnostics. Attendees are encouraged to bring plant data for group discussion and analysis. Common topics will be covered as well as reactor coolant chemistry and radiochemistry, condensate chemistry, balance of plant chemistry, demineralizer and filtration performance, start up and shutdown chemistry, corrosion concerns, and data evaluation techniques.

WHO SHOULD ATTEND

Chemists and Engineers who desire a practical knowledge of Boiling Water Reactor operational water chemistry. This core course is designed for chemistry personnel that have a basic understanding of plant operation and plant systems, focusing on the essentials of reactor water, condensate and processing equipment used in BWR water chemistry operations.

EVENT DETAILS

Event Date
Monday October 31st – Friday November 4th

Duration
8:00 a.m. to 4:00 p.m. Friday 8:00 a.m. to 12:00 p.m.

Individual Price
$2,200 (Includes light breakfast and lunch) Includes BWR Operational Chemistry Handbooks

Location
Hatch Energy Education Building
11028 Hatch Pkwy N, Baxley, GA 31513

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Structural Integrity Associates | News and Views, Volume 51 | Acoustic Emission Testing Streamlining Requalification of Heavy Lift Equipment

News & Views, Volume 51 | Acoustic Emission Testing

STREAMLINING REQUALIFICATION OF HEAVY LIFT EQUIPMENT

By:  Mike Battaglia and Jason Van Velsor

Structural Integrity Associates | News and Views, Volume 51 | Acoustic Emission Testing Streamlining Requalification of Heavy Lift Equipment

Figure 1. Heavy lift rig attached to reactor head in preparation for removal.

BACKGROUND
Proper control of heavy loads is critical in any industrial application as faulty equipment or practices can have severe consequences.  The lifting technique, equipment, and operator qualifications must all meet or exceed applicable standards to ensure industrial safety.  The significance of heavy lifts at commercial nuclear facilities is, perhaps, even greater.  In addition to the consequences of an adverse event that are common to any industry (bodily injury or human fatality, equipment damage, etc.), the nuclear industry adds additional challenges.  Such an adverse event in the nuclear industry can also affect (depending on the specific lift) fuel geometry / criticality, system shutdown capability, damage to safety systems, etc.  One example of a critical lift in nuclear power facilities is the reactor vessel head / reactor internals lift.  

The requirement to inspect the heavy lifting equipment for structural integrity is prescribed in NUREG-0612, Control of Heavy Loads At Nuclear Power Plants, as enforced by NRC Generic Letter 81-07. The aforementioned NUREG document describes specific requirements for special lifting devices.  The requirements prescribed include: 

  • Special lifting devices are subject to 1.5X rates load followed by visual inspection, or
  • Dimensional testing and non-destructive examination (NDE) of the load bearing welds

In the case of the former requirement, it can be difficult or even dangerous to test these lift rigs, which are designed to carry over 150 tons, at a factor of 1.5x.  In the case of the latter requirement, employing the more traditional NDE techniques of MT, PT, and UT to inspect the lift rigs can be costly (both in terms of labor and radiological dose) and time consuming, in terms of impact to outage critical path, depending on when the inspection is performed.  In PWRs or BWRs, inspections are performed in the reactor containment, or radiation-controlled area, and are typically only performed during the outage.   

Ultimately, the NRC requires licensees to determine how they will comply with the NUREG requirements.  One method that has been adopted (primarily by PWR plants) is Acoustic Emission (AE) testing.  AE testing is a non-destructive testing process that uses high-frequency sensors to detect structure-borne sound emissions from the material or structure when under load.  The process detects these acoustic emission events and, based on sensor locations and the known sound velocity and attenuation, can identify the approximate location of the sources or areas of concern.  If such areas are identified, based on analysis of the data captured under load, those areas must be further investigated to characterize the indication.  Such additional techniques may include surface examination (MT or PT), or volumetric UT to precisely locate, characterize, and size any indications.  

Employing an advanced technique such as AE can significantly reduce the time required to perform this evolution, also reducing both the cost and dose associated with meeting the NUREG requirements.  

The original deployment of this method was championed by a utility in the mid-1980’s and has since been adopted by many of PWR plants as the preferred inspection method.  

APPLICATION OF AE TESTING
In 2021, SI began offering AE testing services for reactor head lift rigs, including the qualified personnel, equipment, and tooling necessary to perform this work.  Our first implementation was at a nuclear plant in the Southeast US in the fall of 2021, and additional implementations are contracted in the spring and fall of 2022, and beyond.  

There are several advantages to AE testing that make it uniquely suited for the vessel head (or internals) lift application.  First, AE is a very sensitive technique, capable of picking up emissions from anomalies that cannot be detected by traditional techniques.  This allows for identifying areas of potential / future concern before they are an imminent safety danger.  Second, AE sensors are capable of sensing relevant emissions from a reasonable distance (up to 10 ft or more) between source emission and sensor placement.  As such, AE testing can monitor the entire lifting structure with a reasonable number of sensors (typically less than 20) placed on the structure.  Thus, sensors are strategically placed on the structure where failure is most likely – i.e., the mechanical or welded connections (joints) between structural members.  

This strategic sensor placement has another inherent advantage unique to the AE process.  If an indication is noted, the system has the capability to isolate the approximate source location (generally within a few inches) of the emission.  This is accomplished using a calculation that considers the arrival time and intensity of the acoustic emission at multiple sensor locations.  This is very beneficial when an indication requiring subsequent traditional NDE is noted as specific areas can be targeted, minimizing the scope of subsequent examinations.  

The ability of AE testing to rapidly screen the entire lift structure for active damage growth saves time and money over the traditional load testing and comprehensive NDE approaches.   

Figure 2. Lift rig turnbuckle outfitted with AE sensor.

Finally, and perhaps most importantly, the test duration is minimal and is, effectively, part of the standard process for reactor vessel head removal.  Sensor placement is performed during the normal window of plant cooldown and vessel head de-tensioning, so outage critical path is not compromised.  The actual test itself is performed as part of the head (or internals) lift; that is, when the head breaks from the vessel flange (and maximum load is achieved), the load is held in place for 10 minutes while monitoring for and recording acoustic emission activity.  Each sensor (channel) is analyzed during the hold period and a determination is immediately made at the end of the 10-minute period as to whether the lifting rig structure is suitable for use.  Unless evidence of an imminent failure is observed, the lift immediately proceeds to the head (or internals) stand.  The gathered data are also analyzed on a graded basis.  Depending on the energy intensity of the events detected at each sensor, subsequent recommendations may range from:  ‘Good-as-is’, to ‘recommend follow-up NDE post-outage’. 

The basic process of implementation is:

  • Calibrate and test equipment offsite (factory acceptance testing)
  • Mount sensors and parametric instrumentation (strain gauges, impactors) during plant cooldown and de-tensioning
  • System check (Pencil Lead Breaks (PLBs), and impactor test)
  • Lift head to the point of maximum load
  • Hold for 10 minutes
  • Continue lift to stand (unless evidence of imminent failure is observed)
  • Final analysis / recommendations (off line, for post-outage consideration)

SI VALUE ADD
During our fall 2021 implementation, SI introduced several specific process improvements over  what has been historically performed.  These advances have enhanced the process from both a quality and schedule perspective.  A few of these enhancements are:

COMMERCIAL GRADE DEDICATION OF THE SYSTEM
SI developed and deployed a commercial grade dedication process for the system and sensors.  Often, licensees procure this work as safety-related, meaning the requirements of 10CFR50 Appendix B apply.  The sensors and processing unit are commercially manufactured by a select few manufacturers that typically do not have QA programs that satisfy the requirements of 10CFR50, Appendix B. For this reason, SI developed a set of critical characteristics (sensor response, channel response to a simulated transient, etc.) and corresponding tests to validate that the system components are responding as-expected and can be adequately deployed in a safety-related application. 

Figure 3. Close-up of AE sensor.

EMPLOYING STRAIN GAUGES FOR MAXIMUM LOAD
The arrival time of an acoustic emission at one of the installed sensors is measured in milliseconds. For this reason, it is critical to initiate the 10-minute hold period precisely when peak load is reached. The historical method for synchronizing peak-load with the start of the hold period relied on the use of a stop-watch and video feed of the readout from the containment polar crane load cell.  When the load cell appears to max out, the time is noted and marked as the commencement of the test.  This approach can be non-conservative from a post-test analysis perspective as the data before the noted start time is typically not considered in the analysis. As the strain gauge correlation provides a much more precise point of maximum load that is directly synchronized with the data acquisition instrument, it is more likely that early acoustic emissions, which are often the most intense and most relevant, are correctly considered in the analysis.

REMOTELY ACTUATED IMPACTORS
One of the methods used in AE testing to ensure that the sensors are properly coupled and connected is a spring-loaded center punch test.  This test employs a center punch to strike the component surface, resulting in an intense sound wave that is picked up by all the sensors.  However, this test has historically been performed manually and required someone to physically approach and touch the lifting equipment.  In certain applications, this can be a safety or radiological dose issue and, additionally, can add time to an already time-critical plant operation.  For this reason, SI has introduced the use of remotely actuated impactors to perform this function. The result is equivalent but entirely eliminates the need to have personnel on the lift equipment for the test as this task is performed remotely and safely from a parametric control center.

Figure 4. Strain gauge output showing precise timing of peak load on lift rig.

CONCLUSION
Employing cutting-edge AE testing for your vessel head / internals heavy lift can save outage critical path time, reduce radiological dose, and identify structural concerns early in the process.  All of this leads to inherently safer, more efficient verification of heavy lift equipment.   

SI has the tools, expertise, and technology to apply cutting-edge AE testing to your heavy lifts.  SI is committed to continually improving the process at every implementation.  Improvements in software processing time, and setup / preparation time are currently in-process.  Finally, other potential applications for the method are also possible, and we stand ready to apply to the benefit of our clients.

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Structural Integrity Associates | News and Views, Volume 51 | Turbine Unit Trip and Event

News & Views, Volume 51 | Turbine Unit Trip and Event

Recovery Best Practices

By:  Dan Tragresser

When a unit trips or experiences an event, the site will incur costs associated with the loss in production, regulatory penalties, and, if applicable, outage scope, hardware replacement, and the purchase of make-up power.  These costs can drive the priority of returning to service to quickly become the only priority.

Structural Integrity Associates | News and Views, Volume 51 | Turbine Unit Trip and EventWith the reduction in staffing at power plants over the past 2 decades, many traditionally routine engineering and maintenance tasks have fallen by the wayside.  With limited resources, operations and engineering personnel must focus their time and efforts based on priority.  Quite often, keeping a unit online or quickly returning a unit to service will take priority over continuous improvement actions such as investigations and root cause analysis.

When a unit trips or experiences an event, the site will incur costs associated with the loss in production, regulatory penalties, and, if applicable, outage scope, hardware replacement, and the purchase of make-up power.  These costs can drive the priority of returning to service to quickly become the only priority.  Unfortunately, the review of event operational data, event precursors, and the collecting evidence through the unit disassembly very often fall below the priority of returning to service.  Collecting or re-creating evidence after the fact is nearly impossible.  This lack of priority often results in a lack of understanding of the root cause of the trip or event.  

Within large, complex plants and turbomachinery, trips or minor events are common, but are rarely isolated, one-off events.  Many trips and events are repetitive in nature, and worse, are early indications of a more serious event to come.  While the cost of delays in returning to service may be high, the cost of not solving the root cause may be orders of magnitude higher, particularly if a failure event happens a second time.

Focusing on unit trips, best practices include:

  • Hold regular, cross functional trip reviews.
  • If available, consider holding reviews across similar sites within a parent company.
    • Utilize knowledge and solutions that may already have been developed.
  • Trend trip events and frequency over a 1-to-3-year period.
    • Measure the success of prior projects based on the reduction of occurrences or elimination over a multi-year period.
    • Trips may be seasonal in nature and re-occurrence may span timeframes greater than one year.
  • Review each trip as a near miss and assess potential consequences that may not have occurred this time.
  • Consider including trip investigation in site or corporate level procedures and celebrate successes.

Turbine Blade Failure

Focusing on unit events, the cost of an event requiring an outage and hardware replacement, not including make-up power purchase, can very quickly escalate to millions of dollars.  Compare that cost to the cost of a dedicated, independent resource for the duration of time required to perform a comprehensive investigation.  Also, consider the cost of the investigation versus the cost of reoccurrence, or a similar event with more serious consequence.  The cost of the resource and investigation will almost always be in the noise of the overall cost.  Best practices include:

  • In nearly all cases, site and outage resources will be dedicated to the speedy rehabilitation of the unit.
    • Critical evidence is often lost or destroyed, unintentionally, based on the need to return to service quickly.
    • A dedicated, independent resource provides the best option to ensure that useful evidence is collected.
  • Assign a dedicated, independent resource to collect and review data and findings.
    • If a site resource is not available, borrow from a sister site or corporate team, ideally someone with an outside perspective and not necessarily an expert in the field.
    • Consider an external independent resource such as an industry consultant.
    • It will likely require a team to complete the overall root cause analysis, however, the likelihood of success will be much greater with facts and details being collected by a dedicated resource.
  • Initial steps as a dedicated, independent resource:
    • Ensure a controller and DCS data and alarm logs backup is completed before they time out.
    • Interview individuals that were on site at the time of the event and or in the days prior.
    • There is no such thing as too many pictures. It is common to find a critical link or detail in the background of a picture taken for another reason.
    • Clearly articulate hold points at which the independent resource will require inspections or data collection through the disassembly process.
    • Collect and preserve samples and evidence.
  • Where available, utilize other fleet assets to enable a detailed causal analysis with corrective and preventative actions.
    • Demonstrating a commitment to fleet risk reduction can minimize impacts with regulators and insurers.
  • Once an event occurs, those limited resources will be fully occupied. Creating a plan at this point is too late.
    • Discuss including the cost of an investigation into an event insurance claim with site insurers and what their expectations would be to cover the cost.
    • Maintain a list of resources, internal and external, to call upon as dedicated, independent resources.

Identifying the root cause of an event might be cumbersome, but far less cumbersome than dealing with the same type of event on a recurring basis.

Structural Integrity has team members and laboratory facilities available to support event investigations and to act as independent consultants on an emergent basis.

View News & Views, Volume 51

Attemperator Monitoring with Wireless Sensors

Attemperator Monitoring with Wireless Sensors

Risk and Cost Reduction in Real Time

Jason Van Velsor, Matt Freeman, Ben Ruchte

Installed sensors and continuous online monitoring are revolutionizing how power plants manage assets and risk by facilitating the transformation to condition-based maintenance routines. With access to near real-time data, condition assessments, and operating trends, operators have the opportunity to safely and intelligently reduce operations and maintenance costs and outage durations, maximize component lifecycles and uptime, and improve overall operating efficiency.
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But not all data is created equal and determining what to monitor, where to monitor, selecting appropriate sensors, and determining data frequency are all critical decisions that impact data value. Furthermore, sensor procurement, installation services, data historian/storage, and data analysis are often provided by separate entities, which can lead to implementation challenges and disruptions to efficient data flow.

To provide our clients with a simplified implementation option that expedites the transition of data into intelligence, SI has developed SIIQ, a turnkey monitoring solution consisting of:

  • Assessing the most appropriate (e.g. highest risk) locations and method for monitoring
  • Multipurpose wireless sensor network
  • An independent data transmission infrastructure
  • PlantTrack™ visual database integration
  • Customizable automated alerts
  • Automated engineering insight

While there are many applications in which effective monitoring can be used to more efficiently manage the operation and maintenance of passive assets, such as high energy piping, attemperator management is one specific application that clearly demonstrates the value that can come from an effective monitoring program.

Industry Issue
Attemperators (or desuperheaters), which reduce steam temperature using a water spray, are one of the most problematic components in combined cycle plants. There are several attemperator designs and configurations, but all are potentially vulnerable to damage. If the causes of damage are not addressed early, cracking and steam leaks can occur, leading to costly repairs and replacements. As is typically the case, currently installed data transmitters (pressure taps and thermowells) are located far downstream/upstream and cannot detect local transients that would suggest events like spraywater impingement, pooling, etc. The main challenge is that these events can lead to damage that often goes undetected until it is too late because the damaging temperature transients are not detected by standard plant control instrumentation. Without this local temperature data, it can be hard to predict when re-inspections/other mitigation steps should be pursued.

Monitoring Equipment/Capabilities
To better characterize local temperature events and provide early indication of non-optimal attemperator operating conditions, SI offers a combination of software and hardware components that can be implemented with a range of services from monitoring, detecting, through diagnosing. At the root of these services is the need to collect data from locally installed thermocouples. While some plants chose to run the signal through the data historian and then transmit to SI for processing, an alternative is to use our wireless sensor network to collect and transmit data. SI’s wireless sensor network consists of two primary components: (1) a sensor node that collects the sensor data locally and transmits it wirelessly to (2) a gateway that transfers the data to the cloud.

Figure 1 shows an image of SI’s data collection node, highlighting several of its features. Each node has multiple sensor channels and is capable of collecting data from a variety of sensor types. For the case of temperature monitoring, up to nine different standard thermocouples can be connected to a single node. Additionally, each node is battery powered and is available with an optional solar charging kit for outdoor installations. Furthermore, the data acquisitions nodes are weather-proof and designed to be installed in exposed locations.

As shown in Figure 2, the data acquisition node is installed locally and all thermocouples are hardwired to the node. The node then transmits the data wirelessly to the installed gateway using a proprietary 900MHz wireless protocol. The data collection and transmission frequency is adjustable based on the requirements of the application.

The data from all installed nodes are transmitted to a locally installed wifi/cellular-enabled gateway, which stores the data on a local database until the data is successfully transmitted to a cloud database. Serving as the edge connection to the web, the gateway can be configured to use a cellular network, eliminating the need to connect to any plant networks, or it can be configured with a plant-wide wifi network, if available and accessible. The location of the gateway enclosure is flexible as long as it is within ~1000 ft of all installed data collection nodes.

Figure 1 – Wireless data collection node.

SIIQ/PlantTrack App
Once transmitted off-site, data can be accessed through SI’s PlantTrack software (part of the SIIQ. PlantTrack provides a suite of real-time event and damage tracking applications for common plant components: piping, headers, tubing, attemperators, etc. These applications interface to common DCS / Historian systems allowing for easy implementation, including review and analysis of historical data where that exists.

For Attemperator damage, tracking of temperature differentials with strategically placed TCs provides a means to quantify the number and accumulation of thermal transient events. The signals from the TCs are analyzed to log temperature differential events exceeding some threshold, providing valuable data that can be used to target inspections and plan outage scopes more efficiently. Our software can be configured to provide email alerts when certain magnitude events occur or based on trends in temperature events. Optionally, if PlantTrack Online is connected to the site data historian, SI can fully implement the PlantTrack Attemperator Damage Tracking module, which uses additional sensor data to aid in diagnosing and trending attemperator damage. Actual diagnoses and recommended remediation involves one of SI’s experts reviewing the data. This is made much easier with all the necessary data being compiled automatically within the PlantTrack system. Typical service includes reviewing the data on a periodic basis (e.g. quarterly) and providing a summary of damage events, likely causes, and recommended actions.

Figure 2 – Wireless sensor network configuration.

Figure 3 – Thermocouple data display in PlantTrack.

Figure 4 – Example automated email alert.

To provide some context, the following information provides two (2) case studies of continuous monitoring where some value was realized.

CASE 1:  Bypass spray water stations (Maryland)
Finding: Noted variances in warm-up line functionality and changes to the circumferential temperature differentials/upshock and downshock of the piping.

A select combined cycle plant (2×1) recently experienced a through-wall leak at a girth weld on one of the HRSG’s hot reheat to condenser bypass line. A ring section containing the failed girth weld was removed and submitted to SI’s Materials Lab in Austin, Texas for review. The examination indicated that the crack was consistent with typical thermal fatigue damage, which is the expected damage mechanism for the area considering the proximity of a spray water station. SI recommended that the plant install local thermocouples (TCs) to assess the magnitude of transients experienced during load change events and normal operation – recommendation was made to instrument all 4 areas (2 hot reheat bypass, 2 high pressure bypass). SI also implemented our proprietary wireless sensor network where a node collects the TC data and transmits it wirelessly to a gateway that transfers the data to the cloud (Figure 5). Understanding the transients is the necessary first step, then evaluating/changing the logic, and follow-up with pertinent NDE inspections to ensure there is an understanding of the potential geometric factors here that could exacerbate any issue.  If follow-on inspections find damage then the plant may also consider FEA/fracture mechanics to assess the timing of run/repair/replace options. It is also important to mention that the failed hot reheat bypass girth weld prompted the installation of a new spray water probe assembly to be completed at a later outage.

Figure 5 – SI’s wireless node at the select combined cycle facility that has TC sensors connected.

SI performed a high-level review of the TC data pre- and post-installation of this new spray water probe assembly during a particular outage and also examined all of the bypass location temperature data:

  • Pre-outage (data in Figure 6 shows 10/28/2020 @ ~5:20AM EST)
    • Warm-up line doesn’t appear to be operational – data is similar to post-outage data for the other hot reheat bypass line (has not failed)
    • Several ‘transient’ periods show steady rates of temperature change
      • Sides of the pipe – ambient to ~750-850F and back down to ambient over 20-30 min period
      • Top/bottom – ambient to ~275-400F and back down to ambient over 20-30 min period
      • >400-500F differentials around the circumference

Figure 6 – Pre-outage data for the hot reheat bypass system that experienced a failure.

  • Post-outage (data in Figure 7 shows 12/17/2020 @ ~10:50AM EST)
    • Warm-up line appears to be operational – now differs from the other HRSG hot reheat bypass (warm-up line appears to be malfunctioning/not in operation)
    • Several ‘transient’ periods show much more prominent upshock and downshock (~275F/min in the plot below)
    • Sides of the pipe – steady from ~700-750F
    • Top/bottom – steady from ~700-750F, but then experience differentials after prominent upshocks and downshocks before settling out
      • >250-300F differentials around the circumference
  • Consensus on the pre- and post-outage data
    • Temperature differentials for the hot reheat bypass that failed appear to have improved from pre- to post-outage with a new probe assembly, but now with a functional warm-up line there are periods of more prominent temperature transients
      • Differentials around the circumference still exist
    • Spray nozzles can still be optimized

Figure 7 – Post-outage data for the hot reheat bypass system that experienced a failure.

CASE 2:  Reheat interstage spray water stations (Texas)
Finding: Identified unevaporated spray water is present during cold starts and load changes. Resulting inspections identified prominent cracking of the piping in the vicinity of the spray water probe assembly.

A select combined cycle plant (2×1) has a reheat interstage line that was previously identified by plant personnel as having a prominent sag with the low point located near the desuperheater in 2017. A liner is indicated on the drawing, which should protect pipe ID surface from spraywater. However, SI performed a high-level operating data review and did some localized NDE of this region (January 2018).

This initial data review considered existing transmitters (pressure, temperature, valve positions, combustion turbine loads, etc.) and found that there is some indication that the reheater desuperheater spray control valve is not fully closed, or may be leaking under some conditions. A leaking spray water valve could contribute to pipe bowing as that would make the bottom of the pipe colder than the top. Normally, if the desuperheater piping is able to flex, then when it is cold on the bottom and hot on the top it will hog (bow up). If, however, the piping flex is constrained so it cannot hog, then the pipe remains horizontal and a significant tensile stress is developed in the bottom of the pipe. This causes the pipe to effectively “stretch” on the bottom so the bottom is longer, and over time this can lead to a bow down. During the warm start there are a few minutes where the desuperheater pipe is at or below saturation temperature, which could result in condensation in that line. There could also be spray water that has collected in the line prior to startup that takes some time to evaporate. In either case the result would be a top to bottom temperature difference in the pipe.

From the inspection side there were no major issues noted, but a recommendation was made to install surface-mounted thermocouples (TCs) at pertinent locations to assess the magnitude of thermal transients experienced during load change events and normal operation. Plant personnel installed 5 TCs (2 upstream of the liner/2 downstream of the liner at the top and bottom of the piping; 1 at the extrados of the downstream bend). Plant personnel routed the TC sensors to their data historian (PI) for continuous monitoring.

SI was then requested to perform a review of this second dataset to determine if there are problematic temperature differentials within this line (October 2020). The data indicated that during the cold start and at low load operation (Figure 8 and Figure 9), the spray flow is not fully mixed and saturated steam is impinging on the top of the pipe downstream of the spray. This prompted another inspection (January 2021) now that saturated steam was identified and also prompted a review of the liner/probe assembly port.

This particular inspection identified circumferential indications consistent with ID-initiated thermal fatigue noted within liner boundary. This damage started at the downstream side of nozzle port and continued axially for ~5’ before dissipating and was located from 10:00à2:00 (top circumference). The through-wall depths were prominent – through-wall failure and several other locations with 40%+ (some rough measurements of ~60-80% through-wall noted, as well). It appeared that possible condensate may be inadvertently leaking around the nozzle assembly and entering the reheat interstage line through the nozzle port/flanged connection – once it hits a little bit of steam flow in the line it may push this into the void between the liner and ID of the pipe.

In areas that were originally slated for inspection (exit of the liner, downstream extrados of the bend), no findings were noted. The unevaporated spraywater that was identified by the secondary data review is obviously not ideal, but damage development is driven by the magnitude of the temperature transient and the cycle count and does not appear to have manifested in service damage at this stage. Continuous monitoring is advisable.

Figure 8 – TC and existing transmitter data for a cold start that revealed unevaporated spray water in the reheat interstage line.

Figure 9 – TC and existing transmitter data for a load change that revealed unevaporated spray water in the reheat interstage line.

(Summary)

The crucial aspect in assessing the performance of these systems with spray water stations is being able to determine the magnitude and frequency of thermal transients. With the nearest temperature transmitters (thermoelements) typically located far downstream, local thermal transients at the conditioning valve and desuperheaters are often not detected. Surface-mounted thermocouples routed to the data historian/digital control system (DCS) or collected wirelessly help to evaluate temperature differentials around the pipe circumference and at geometrical impingement points. This, in conjunction with existing transmitters, allows for early detection of potentially damaging events so that appropriate mitigations (maintenance, logic updates, etc.) can be performed before costly repairs are required.