Onsite – Page 53 – Combined Cycle Journal

How to straighten a bowed steam-turbine rotor

By Team-CCJ | February 4, 2022 | 0 Comments

When you’re sick, or something seems “off,” what do you do? Many people search the web, often arriving at a WebMD, Mayo, or equivalent site, for some initial information. If symptoms persist, you go to your primary-care physician. The doc may tell you to see a specialist or even a surgeon.

Thankfully, when your steam turbine seems “off,” and you suspect the rotor, you can get “integrated care” from the 500 folks at MD&A, including 200 seasonal traveling turbine experts. Who says doctors don’t make house calls?

Think of the “Bowed Rotor to Straight Rotor” presentation by Rob Kilroy in MD&A’s Spring 2021 Webinar Series, summarized here, as WebMD. If the turbine rotor needs an official diagnosis, MD&A will send inspection specialists to your site. If the diagnosis suggests repairs, the company will handle those as well.

If you are recording a gradual increase in rotor vibration over a long period, it may be time to listen up. The rotor may be bowed, caused by persistent asymmetrical heating or cooling of the shaft. Pre-1960s turbines rarely experienced bowing. Today’s longer, more slender rotors with a reduced number of bearing pedestals and more aggressive operating parameters are more susceptible.

The MD&A crew is seeing around a dozen bowed rotors each year. That may not seem like a lot, but given the damage a bowed rotor can do, it’s best not to find out the hard way.

In the webinar, Kilroy explains rotor bowing is defined by the total indicated reading (TIR). If the TIR is less than 0.03 in., the bowing is minor, if between 0.04 and 0.015 in., it’s moderate, and above 0.016 in., consider it severe. Severely bowed rotors typically cannot be balanced, and will require an engineered straightening solution.

The turbine/generator repairs engineer delineates three categories of straightening options, once the detailed in-casing and disassembly inspections are completed: Machining/throwing of journals, stress relief/heat lathe, and thermal straightening (photo). The last two typically do not require resizing of the bearings.

Best of all, Kilroy reviews seven case studies, the first three on the cusp of severe with max TIRs of 0.015. In general, the “surgeries” MD&A performed return the rotors to a TIR of between 0.001 and 0.005. In one case, a rotor with “all kinds of problems” and a 0.007-in. TIR at the turbine end and 0.053 at the generator end, MD&A’s solution reduced the TIRs to 0.001 in. at both ends.

Rotors from a variety of manufacturers are featured in the case studies. Frequently, the rotor was subjected to multiple straightening options and ancillary machining and component replacements. You’ll understand the innovative thinking that’s required once you watch the video (users only).

What GE told STUG2020 attendees about its steam turbines

By Team-CCJ | February 4, 2022 | 0 Comments

Matt Foreman, platform leader, Combined-Cycle Steam-Turbine Services, opened the GE Day program at the 2020 virtual meeting of the Steam Turbine Users Group (STUG) with an overview of the topics to be discussed, including: fleet updates, valve and turbine-casing cracking, valve upgrade experience, D11 rotor bow, assessments to improve operability and reduce O&M spend, and performance improvement. Highlights follow. The full presentation recordings can be accessed by approved GE customers on the MyDashboard website.

If steam turbines fall under your responsibilities, be sure to register for the STUG 2021 annual meeting in St. Louis, taking place August 23-27.

TIL, GEK, and fleet updates

Mike Jones, service manager for ST products, and Jamie Anderson, ST system integration leader, stressed the importance of these two Technical Information Letters:

    • TIL-2010 recommends endoscopic inspection and NDE of the radial inlet vane at the next scheduled outage to identify possible deformation and/or cracking, which can be caused by a clearance reduction attributed to scale buildup. A borescope inspection ahead of the outage was suggested.
    • TIL-1886-R1 requires removal and NDE of finger-dovetail L-1 buckets after 30 years of service to inspect for stress corrosion cracking in the dovetail area.

Recent D11 shell and valve casing findings

Dave Welch, consulting principal engineer for ST product service, shared recent HP/IP shell casing findings and experience in mitigating horizontal-joint leakage, plus N2 packing-head experience and valve-casing findings.

He stressed the cleaning, inspection, maintenance, and repair of casing cracks as essential outage activities to prolong the life of HP and IP shells. Photos of casing findings and typical locations of occurrence provide valuable user perspective. TILs 1748 and 1749 suggest machining actions to address casing stress issues, which are impacted by creep and low-cycle fatigue.

Horizontal joint leaks are not a major fleet concern, noted Welch. They are caused, he said, by creep relaxation of joint studs and nuts and by localized casing distortion from thermal- and pressure-induced stresses. Repair options are presented.

N2 packing-head (PH) replacement benefits and experience were summarized for attendees. Users were referred to TILs 1627, 1748, and 1749 regarding shell and N2 PH fit modifications released about 10 years ago. Welch said GE has successfully implemented about 50 modified packings within the D11 fleet. He added that the OEM’s reconfigured N2 packing head has reduced premature failures of the shell and the PH throughout the fleet.

Casing cracking on old-style main stop and control valves (MSCV) has occurred before 15 years of service, Welch continued, recommending blast-cleaning and inspection for indications at every minor outage. Grind and blend, or machine-out, small cracks once they are found to minimize the need for a weld repair later.

The OEM’s Next-Gen ST valve experience

Welch opened his second presentation by explaining that Next-Gen is a name change for the “digital-valve” moniker used previously. Reason: The improved offering goes beyond digital with robust hardware material and geometry improvements. The enhanced hardware can enable minor-outage interval extensions from three to six factored years.

There are two standard product offerings for MSCVs and combined reheat valves (CRVs):

    • Package 1 targets 7.5-, 9.25-, and 11-in. valves with modern actuators and no casing cracks, primarily addressing issues related to the internals—such as stem sticking and solid-particle erosion (SPE). Installations, which can be done during a minor outage, thus far reveal no SPE of valve stems. Return-to-service issues—wiring and erratic behavior—on two valves—were resolved quickly. In both cases, the actuators had not been replaced. Eight units now have Package 1 installed with the first unit accumulating hours since 2017.
    • Package 3 addresses issues related to valve casing cracks and includes a new actuator. Target is 9.25-in. lower-chamber valves and CRV links and lever hydraulics. Valves for the first replacement project in October 2019 were installed in less than a month.

Rotor-bow detection and corrections

John Sassatelli, consulting engineer, repair development, opened his presentation with a survey, to help focus his presentation on user needs. The question: Where is your plant regarding ST rotor bowing? There were four possible answers: (1) I don’t think my rotor is bowing; (2) I think my rotor is bowing and I’m monitoring it; (3) I have taken some action to address rotor bow, and it’s working; and (4) I have taken some action; however, it looks like the bow is returning.

Nearly 60% of the respondents did not think their rotors were bowing.

Sassatelli then outlined his highly informative and practical presentation, one that all users with rotor involvement likely would benefit from (access it at GE’s MyDashboard.com). He covered rotor-bow detection (What is it? What to trend?), causes (Why does it happen? What are the system effects?), and management (Managing the factors contributing to rotor bowing, plus issue remediation and intervention.).

Runouts taken with the unit out of service are critical to understanding what’s causing the bow, the consulting engineer said. He then put up a slide of a D11 rotor with three typical curves developed from runout data—one showing a bow centered at the HP-steam inlet, one with a “kink” at the reheat-steam inlet, and one illustrating a bow distributed along the length of the rotor (parabolic shape).

If you suspect your rotor may have a bow, Sassatelli said you want to know if the bow is temporary or permanent and if the vibration response is trending up or down over the unit’s service history. He suggested reviewing the first-critical-speed response over the time horizon for which data are available. You also want to see if the shutdown critical normalizes the thermal effects of startup.

Three well-illustrated case histories were presented to facilitate understanding the vibration signatures of bows. But wait! Things other than a bow can produce similar signatures (misalignment, oil/steam whirl, mass loss, rotor crack, for example) and you should rule them out before pursuing a bow solution. Suggested reading: GEK 89610.

Sassatelli then asked the group which came first on their units: rubbing or bowing? More than two-thirds of the respondents said “rubbing.” He then offered several charts to help owner/operators answer the question: Does rubbing cause bowing or vice versa? Vibration plots of cold and warm starts show the latter is less likely than the former to produce vibrations of sufficient magnitude to initiate a turbine trip.

Although a warm start does not give the same high vibration numbers as a cold start, Sassatelli continued, it does seem to correlate with accumulated damage. The riskiest timeframe for light rubbing, he said, is a warm start 24 to 48 hours after shutdown.

The impact of insulation condition was factored into the speaker’s comments on rubbing. The increasing temperature deviation between the upper and lower casings over time in the area of the HP and RH steam inlets, he said, generally can be attributed to insulation deterioration. The delta T contributes to casing distortion conducive to rubbing.

The pros and cons of various rotor and system interventions closed out Sassatelli’s presentation. They provide of checklist of options for owner/operators to consider for mitigating bowing concerns.

Analyzing the data from your combined cycle

Principal Engineer Peter J Eisenzopf’s goal was to share methods for turning operating data into information that can be used to make better O&M decisions. He, like the previous speaker, began with a short survey question to help focus his remarks on user needs. The question: Which steam-turbine components/systems drive the most emergent work? The four choices: Turbine valves, rotors, casings, and accessories and balance-of-plant equipment. If “turbine valves” is your answer, you’re among the majority. Two-thirds of the respondents, in round numbers, agreed with you.

Eisenzopf then provided a useful checklist of items the OEM uses to gather information of value so you can better manage your unit and outages. The variables discussed and illustrated in the presentation included the following:

    • Lifetime mission mix. The chart provided for one D11 plots the HP bowl metal temperature at the time of turbine roll for all lifetime starts, allowing plant staff to identify easily changes in mission over the years. Examples: When the plant was in peaking service, when warm starts predominated, etc.
    • Lifetime shutdown hours preceding an ST roll (an alternative to HP bowl temperature to define the type of start). Fleet data indicate the most common starts, in decreasing order, occur at eight, 32, and 56 hours, and in 24-hr increments beyond that. The message: When specifying guarantees for new units, owners should consider asking the OEM for the start times associated with these specific shutdown durations, plus dead cold. Traditionally, start-time guarantees for new units most often have been specified at eight, 48, and 72 hours.
    • Percent cyclic tracking. GE invented the parameter “percent cyclic” because simply tracking the number of starts does not include sufficient information for lifetime evaluations. Eisenzopf said units with similar percent-cyclic missions may also have similarity in the features which require maintenance. Understanding this with GE’s help could be valuable in both outage planning and in designing an operational profile to maximize asset value.
    • Lifetime operating hours are tracked by virtually all plants because of its value in inspection and maintenance planning. But the speaker said tracking factored hours is more valuable because it is condition-based.
    • Transient ST load profiles. Eisenzopf explained GE’s transient-data viewer tool which enables you to chart important turbine operating parameters—such as start time, which can help operators reduce start times and lower startup cost.
    • ST rotor cyclic life per start/shutdown cycle helps in reducing start times. It is particularly valuable for quickly assessing the impact of changes to startup logic/procedures on rotor life consumption.
    • Cooldown upper-to-lower shell metal temperature-difference tracking allows operators to assess the relative quality of their insulation, the OEM having fleet-wide data for comparison. Eisenzopf stressed the importance of insulation quality in minimizing casing distortion. The methodology discussed can be used by plant staff for evaluating the work of contractors in replacing insulation after an outage.
    • Startup transient efficiency tracking. GE invented the “transient efficiency” metric to measure/quantify startup quality. In the example provided by the speaker, plant was able reduce the start time by more than an hour with life consumption equal to or lower than the baseline number.

Several more parameters—such as steam-to-metal temperature matching at ST roll—also are discussed in Eisenzopf’s presentation available at MyDashboard.com. While they all enable better decision-making, their measurement and tracking may require instrumentation and data collection capability not currently available at your plant. Performance improvement, like most everything else, has a cost, but it typically is a relatively small percentage of the financial gain.

One way to launch a performance improvement initiative at your facility might be to review the presentation, determine what variables you are not now tracking and begin doing so, identify other parameters you believe have value in tracking, and determine what equipment and controls changes are necessary to make this happen. Then do it. Your GE rep can help, of course.

Combined-cycle ST performance improvement strategy, tradeoffs

Jim Stagnitti, leader, application and requisition engineering, began by reviewing the reasons owner/operators pursue performance-improvement initiatives—extend maintenance intervals, improve reliability and/or flexibility, for example—and the considerations involved in decision-making—including cost, desired remaining unit life, and operating profile.

He then explained the value of a so-called “opening assessment” to make recommendations for repairs during an upcoming outage, both structural (impacts reliability) and thermal (impacts performance). A closing assessment also is necessary, the group was told, to verify the as-left condition of the unit.

A highlight of the presentation was an overview of what’s involved in upgrading your ST with a new rotor. Simply put, a typical scope is full steam-path replacement—that is, bucketed rotor, diaphragms, packing heads, and seals. This likely would be done to accommodate an increase in steam flow attributed to a gas-turbine uprate, increase in duct-burner capacity, and/or HRSG upgrade. The benefits of this approach include the following:

    • Avoid emergent work and the risk of outage extensions.
    • Restart the maintenance clock with new and clean replacement parts.
    • Improve heat rate

An economic analysis presented supports the value of rotor replacement. The case study showed steam-path replacement value is positive within three years and increasing over time.

EPRI reports offer a short course on delamination of hardfacing and how to avoid it

By Team-CCJ | February 4, 2022 | 0 Comments

EPRI led a research effort from 2013 to 2015 to identify contributing factors to the large number of hardfacing failures—a/k/a delamination or disbonding events—experienced industry-wide. The project purposely engaged stakeholders in the valve supply chain with both users and valve manufacturers sponsoring the effort. Content summaries of the three technical update documents issued in 2015 as a consequence of this effort are below. They are available at no charge to select EPRI members and for a fee to others. To purchase, contact the EPRI Order Center at 650-855-2121 or orders@epri.com.

Investigated failures occurred primarily in valve components (disc, seat, and/or stem) fabricated from CrMo Grade 91 or 400-series stainless where a cobalt-based hardfacing material (Stellite) was directly clad on the base metal. Failures were observed in components where the stated operating temperature was a nominal 975F or higher.

EPRI continues to investigate and update its guidance on the subject. The latest iteration of this ongoing research effort is being led by Dan Purdy (dpurdy@epri.com), a senior technical leader in the organization’s Materials and Repair Program. Purdy now is in the early stages of integrating the first report in the three-part series into a more encompassing large-bore valve-body specification.

“Guidelines and Specifications for High-Reliability Fossil Power Plants: Recommendations for the Application of Hardfacing Alloys for Elevated-Temperature Service,” EPRI product 3002004990, 30 pages.

Cobalt-based hardfacing alloys are used to protect sealing surfaces in high-temperature valve components primarily because of their resistance to wear. Inspection of ex-service valve components has revealed early cracking and disbonding of the hardfacing from the substrate material. Analysis identified the formation of undesirable hard, brittle intermetallic phases in an intermixed zone typically between the substrate and the hardfacing layer.

Although the degree of this first weld pass dilution can affect the extent and kinetics of embrittlement, it is desirable to remove the possibility of the undesirable phase formation entirely through the application of nickel-based-alloy butter layers that do not show the tendency of phase transformation at any level of dilution with the substrate or cobalt-based hardfacing

Report’s objective is to provide scientifically based guidance in the engineering, quality control, and inspection of welded joints between ferritic valve components and cobalt-based hardfacing to avoid delamination in service.

“Experiences in Valve Hardfacing Disbonding,” EPRI product 3002004991, 96 pages.

Evaluations of service history and failed ex-service components have led to an understanding that metallurgical changes within the microstructure during welding and high-temperature service exposure contribute to disbonding. Cracking has been shown to prefer bands of unexpectedly hard layers in the weld deposit, and there is evidence of the formation of the brittle intermetallic Sigma phase in those regions. The solution appears to be not one of process—that is, dilution—control, but rather identification of the alloy combinations that remove the possibility deleterious phases will form.

The report discusses the history of hardfacing disbonding as it applies to the power-generation sector of the industry. Included in the timeline are the advances in the state-of-the-art in fabrication, the potential consequences of those changes in processing, a variety of notable failures, and a thorough look at the thermally driven stresses in valve components. Metallurgical analyses of failed components covering a range of material combinations and applications are presented. Many material combinations have been used to varying degrees of success; the report describes the causes of the issues.

 

“Proposed Solutions for Hardfacing Disbonding in High-Temperature Valves,” EPRI product 3002004992, 66 pages.

This third report elaborates on an exhaustive thermodynamics methodology to predict the formation of deleterious intermetallic phases over a range of alloy combinations, and the degrees of mixing among them. The thermodynamic predictions uncovered a wide range of problematic material combinations, as well as several key parameters that lead to metallurgically stable combinations—regardless of the degree of mixing among the constituents. Stitching together these safe combinations creates a layered hardfacing welding procedure that removes the possibility of harmful phases affecting the matrix and leading to disbonding.

These alternative weld solutions were validated through laboratory trials and extended ageing to demonstrate their long-term stability. Laboratory welds that recreated the problematic combinations were observed to begin their transformation, while alloy combinations that were expected to be free of that risk did not harden.

Stellite delamination is preventable, but owner/operators must ‘enforce’ the solution

By Team-CCJ | February 4, 2022 | 0 Comments

Liberation of cobalt-based hardfacing (oft-used Stellite™ being one of these materials) from large Grade 91 valves installed in combined-cycle main and hot-reheat (HRH) steam systems, and in steam turbines, was a hot topic in the industry about a decade ago. With the need for an evidence-based solution, the Electric Power Research Institute (EPRI) assembled a committee consisting of owner/operators and stakeholders in the valve manufacturing supply chain to collaborate on the development of guidelines to mitigate the issue.

Three reports on that effort were released by EPRI in 2015 (see companion article) and the solution identified has prevented disbonding of the hardfacing where employed—at least CCJ ONsite has not identified any cases where the solution has not met expectations. Although there are only five or six years of field experience to validate the successful approach at this time, that’s a big improvement for some plants where delamination had occurred in as little as 12,000 hours of operation.

With a solution available, why is CCJ ONsite covering this topic again? The answer in brief: Not everyone who should know about this relatively recent development is aware of it. Proof of the knowledge gap came by way of a phone call from Aaron Florek of Millennium Power Services, a major player in the valve repair business, who told the editors that his firm recently had repaired valves suffering disbonding at three plants in a three-month period.

Needing confirmation that the old news (delamination) is new again, the editors contacted two technical experts with deep experience on the subject—Kim Bezzant of Utah-based Wasatch Welding Engineering Services and John Siefert, manager of EPRI’s Materials and Repair Program—as well as current users, and power-industry veteran Joe Miller, now industry director for power at ValvTechnologies Inc, which offers an alternative to Stellite hardfacing on the disks, seats, and stems of new steam valves.

All agreed that Stellite disbonding continues to haunt the industry—in large measure because owner/operators generally haven’t been diligent in upgrading their specifications both for new valves and valve repairs to reflect recent experience. It is not sufficient to simply specify that valves be manufactured, or repaired, to meet the requirements of the ASME Boiler and Pressure Vessel Code (for valves within the Code boundary) and ANSI/ASME B31.1 (for valves included with boiler external piping). Recall that these documents prescribe minimum requirements and were developed to ensure that the equipment they address is safe.

They certainly do not protect against the financial fallout from a delamination event that forces your plant offline or prolongs a scheduled outage. With all the changes to grid contractual agreements over the last few years, it is worth reviewing the exposure your plant could have to a valve failure and how much it’s prudent to spend on original equipment and repairs to insure against one.

Remember, too, it’s not enough to simply upgrade valve specifications, you have to monitor the manufacturing and repair practices of the selected solutions providers to ensure they are doing what you have carefully specified in the contract. This can be challenging where offshore vendors are involved. Boiler manufacturers and EPC firms tend to buy foreign, in particular from Korea and India, to reduce their costs and they may be reluctant to monitor contract performance in-person. Such details must be agreed to and understood before work begins.

Many boiler and turbine valves have performed admirably over the years with cobalt-based hardfacing, as well as with other hardfacing materials. But the change to Grade 91 valve bodies and the demanding operating conditions for heat-recovery steam generators (HRSGs) in combined-cycle service have pushed to the limit the technology traditionally used to bond cobalt-based hardfacing to C12A or F91 valve trim. Today’s high steam temperatures required a different methodology for attaching the two materials.

In simple terms, here’s what EPRI’s materials experts learned: Addition of a “buttering” layer of nickel-based alloy—such as Inconel™—separated Stellite and F91 material and prevented formation of an undesirable metallurgical condition in the weld zone between the two metals which is conducive to disbonding.

Plant experience. Florek told CCJ many plants in the country are addressing Stellite delamination issues and there are many more not yet aware of the problem they probably have. The three plants located in the Northeast that Millennium Power provided outage services for in the three-month period (2020) mentioned above illustrate findings typically identified at other facilities. Here are some of the details from those projects:

The first plant, a 2 × 1 H-class combined cycle began operating in 2017. Delamination was observed on six valves associated with the boilers and steam system at that facility—HP HRSG isolation, HP header isolation (a/k/a blending valve), and HRH (hot reheat) header isolation (for isolating one boiler from the other when necessary). The first type was in the European boiler manufacturer’s scope of supply and sourced from Korea, the mixing valves in the EPC firm’s scope came from another manufacturer.

The 14-in., F91 HP boiler valves were specified for service at 2420 psig/1065F. The type of Stellite hardfacing was not specified. What is known is that no buttering layer was used and that the Plasma Transferred Arc Welding (PTAW) process likely was employed for Stellite attachment. The HP isolation and blending valves are of the parallel-slide gate type and suffered Stellite liberation from both the seat rings and discs.

Note that these valves were manufactured before the EPRI guidelines (sidebar) were published. The EPRI findings identified disbonding concerns beginning at steam temperatures of about 975F, possibly even lower, with shorter expected life as the operating temperature increased.

When restarting the plant after the 2020 spring outage, an HP bypass valve on one of the HRSGs stuck open at 80% of full travel. This particular valve had just been retrofitted with a new magnetite strainer modification and reassembled. Inspection revealed hardened material in the valve, begging the question: Where’s this coming from?

Repair of two valves on the boiler (the stuck-open valve and one additional HP valve), plus inspection and removal of debris from the steam system, were priorities. Some of the liberated material had traveled downstream to the steam turbine. It had piled up against the unit’s protective steam strainers and was removed later, in fall 2020. During both outages, a borescope equipped with a magnet was run up through the steam lines to collect any remaining loose debris.

A specialty engineering firm was engaged to analyze the scrap and make recommendations. There were no unexpected findings. That company also confirmed the importance of a buttering layer. Bezzant recommends a buffer layer of ERNiCr-3 (Inconel Filler Metal 82), or an equivalent PTAW powder, to prevent carbon migration into the Stellite.

The affected valves were disassembled and discs and seat rings cut out. Millennium provided new seat rings and hardfacing for the discs consistent with EPRI recommendations and the company’s experience.

Plant personnel continue to analyze the delamination issue and how to prevent it, with assistance from one of the valve manufacturers. One of the questions they are trying to answer: Is there a temperature at which hardfacing of the type currently used and applied becomes impractical? Another: Is the ramp rate or steam temperature the cause of disbonding?

Steps already taken by the plant include modification of its cold-start procedure (more time) and greater emphasis on the use of sparging steam from an auxiliary boiler to keep the unit warm when offline.

Regular inspections of valves are important to assess their true condition. The plant manager suggested that absent leak-by, your valves likely are fine. But it’s probably a good idea to still select one or two valves at random for a thorough NDE inspection during each hot-gas-path outage. Why only one or two valves? Every time you open a healthy valve you run the risk of compromising its integrity.

If your inspection indicates leak-by, immediate action to correct is recommended.

Millennium Power refurbished four HP valves (isolation and blending) on the affected boilers to return the combined cycle to full power as quickly as possible. Work on the valves was completed in-situ a day ahead of the eight-day schedule. Plant’s plan is to address damage to other valves suffering delamination, as necessary, during future scheduled outages.

In preparation for the fall 2020 outage, Millennium got the repair effort on the two HRH blending valves moving before the outage began by making new seat rings in its shop, Florek touting the company’s ability to reverse engineer and typically make any manufacturer’s valve parts in less time than it would take the vendor of record to supply them.

The first step in the repair process was to remove damaged parts and prep the valves for new parts and hardfacing—something Florek says the company has done at least a couple of dozen times to date. Follow key steps in the montage of photos incorporated into Fig 1. He added that sometimes just the hardfacing is damaged, not the basic part. In such cases it’s sometimes possible to remove the coating and reapply Stellite with the requisite butter layer.

Millennium Power’s field service personnel moved in short order from this project to another in the region where two 24-in. parallel-slide gate valves were refurbished within two weeks. Old seats were removed, new seats manufactured with Stellite overlay and Inconel butter layer, and the valves rebuilt, including new actuators. Original seat welds were found broken; one of the seats was severely deformed (Fig 2).

At the third plant in the Northeast that Millennium serviced within the three-month period noted above, a 24-in. wedge gate valve in the HRH system was scheduled for a stem replacement to mitigate packing wear. A new stem was manufactured in the company’s shop and shipped to the site for installation.

When technicians disassembled the valve, Stellite disbonding was found on the wedge and both seats. The owner approved corrective action the next day and Millennium’s field machining crew arrived onsite four days later to remove both seats while concurrently refurbishing the existing wedge in accordance with EPRI recommendations. Seats were replaced, wedge refurbished, and valve reassembled all within 16 days of project start.

Steam turbine. A case study of damage suffered by a 262-MW D11 steam turbine because of Stellite delamination associated with HRSG steam valves was presented at the 2019 meeting of the Steam Turbine Users Group. The clue that something was amiss: Following a routine valve test, operators recognized that throttle pressure had to be increased by 70 to 80 psig above “normal” to maintain desired output—symptoms consistent with possible steam-path fouling or damage.

After weeks of data monitoring and analysis involving personnel from the owner/operator and OEM, a two-week outage was taken. Delamination of Stellite from the seats of HRSG steam valves was confirmed by investigators and a borescope inspection of the turbine HP inlet revealed significant damage to the first-stage nozzle block and buckets.

Three run-versus-repair options were considered for the steamer: repair now (reliability outage); run at reduced load with no cycling permitted, and repair when new buckets arrive; and run until the major maintenance outage planned for some months ahead.

The OEM’s recommendation was to run the turbine until the planned major and order new buckets and diaphragms for the first four stages of the 262-MW unit; plus, monitor the machine for noticeable changes in operation that would indicate additional damage. Also recommended was that the owner implement a program to inspect and replace similar Stellite-hardfaced valve parts exhibiting delamination.

Be aware that Stellite also has disbonded from the seats of steam-turbine valves; guidelines for their inspection are presented in GE’s TIL-1629R1, “Combined Stop and Control Valve Seat Stellite Liberation,” Dec 31, 2010. Thus, the information provided in this document predates the extensive work done by EPRI, and summarized in the companion article, by five years.

Inspection. Industry experience suggests inspection of large steam valves for delamination and other possible issues during the next hot-gas-path (HGP) or major inspection—especially if this has not been done previously. Wasatch Welding Engineering Services’ Bezzant explains that visual inspection will confirm Stellite liberation, dye penetrant testing will reveal cracking not visible with the naked eye, and a straight-beam ultrasonic examination is necessary to identify disbonding that may be occurring but not found by visual or dye-penetrant examination.

But before opening your valves, he suggests you have a game plan for repair or replacement in case you find damage. Failure to plan ahead could significantly add to your outage schedule.

Here are your options if damage is found, according to Bezzant:

    • Replace the existing valve with a new one.
    • Cut the valve out of the line and send it to the manufacturer or a qualified third-party shop for repair.
    • Repair the valve inline.

Owner/operators who have already faced repair/replace decisions suggest that you factor the following facts into your decision:

    • The lead time for new valves may extend beyond a year.
    • Shops capable of doing quality valve work and welding generally have a backlog.
    • Quality repairs are difficult to make inline because of preheat and access requirements.
    • Field-service organizations with the requisite in-situ valve repair experience are extremely busy.
    • There is no industry standard for applying hardfacing, although EPRI’s recommendations for this are supported by those contacted by CCJ ONsite. Manufacturers and repair firms may have other procedures but they should be qualified metallurgically before work begins on your valves. Plus, owner/operators are advised to carefully monitor repair work to the qualified written procedure.

The editors contacted California-based Bay Valve at the suggestion of a user to get an idea of what’s involved in conducting a valve inspection. In two words: A lot. Bay said the company’s standard procedure is to have highly experienced personnel perform visual and dye-penetrant inspections and if cracking or other problem is identified it is referred to plant management, which might decide to expand the scope of the examination.

Preparation for inspecting a 12- to 14-in. HP or 20- to 24-in. HRH valve can take upwards of two days, one of the field supervisors told CCJ ONsite. Actual time depends on the size of the valve, manufacturer, plant constraints, etc. He walked the editors through the rigging and safety measures required to remove a 1-ton handwheel as evidence of some of the difficulties sometimes encountered. Budget another five days to complete the inspection and return the valve to operational condition.

Stellite-free valves. Hardfacing options other than Stellite are used in the industry. They too may have technical challenges and owner/operators should investigate their service histories thoroughly before deciding on what hardfacing material to specify.

ValvTechnologies’ Miller, contacted at the suggestion of an owner/operator with several Stellite-free valves at its plants that have been problem-free for several years save one stem packing leak, discussed the highlights of his company’s IsoTech® design for high-pressure applications.

ValvTechnologies’ parallel-slide gate valves for demanding combined-cycle service rely on the manufacturer’s proprietary RiTech® 31 (80% chromium carbide and 20% nickel/chrome by weight) coating, which is much harder than Stellite 6 (68.5 Rockwell C versus 30 for Alloy 6 at 1000F, a difference that increases with temperature). The coating is applied to critical parts—discs, seats, and guides—in HVOF (high-velocity oxygen fuel) spray booths using a compressive spray technique to achieve high bond strength.

The hard coating on the web guide ensures the discs are kept parallel through the entire valve stroke. As the valve is cycled under differential pressure, the hard surfaces reportedly burnish and polish each other, avoiding the scratching and galling cited by some users not using RiTech 31.

Miller said the company’s new IsoTech hybrid design has a cast A217 C12A short pattern body with welded-on forged end rings (pup pieces) which can be either A 182 F91 or F92 to match the piping-system material. The length of the end rings also can be customized to meet either ASME B16.10 end-to-end dimensions, or be provided longer to allow removal of heat-affected-zone material on valve replacement projects. Expected time for customization to your specific requirements is four weeks or less.

The new valve, characterized by a very low pressure drop, according to Miller, accommodates 12, 14, and 16 in. requirements with the same cast body.

NERC cybersecurity info sharing platform explained at Siemens forum

By Team-CCJ | February 4, 2022 | 0 Comments

During the Siemens Executive Cybersecurity Forum for Electric Power, held virtually June 17, 2021, Manny Cancel, senior VP, North American Electric Reliability Corp (NERC), encouraged electric-power industry stakeholders to share information on cybersecurity threats, vulnerabilities, and experiences through NERC’s E-ISAC (Electricity Information Sharing and Analysis Center) platform.

Cybersecurity alphabet soup is thick enough, and it’s often difficult to see what value many of these cyber organizations and initiatives offer. Nevertheless, it’s good to at least be aware of them and their work on behalf of the industry. This report, available from E-ISAC website, may help you figure that out.

Among other things, E-ISAC runs GridEx, an annual simulated attack scenario to which stakeholder leaders respond as a “play” exercise. The goal is to “engage senior industry and government leaders in a comprehensive discussion of the extraordinary operational measures needed to protect and restore the reliable operation of the bulk power system (BPS).”

On an on-going basis, E-ISAC members work with the relevant government agencies to find patterns and trends in vulnerabilities, threats, and incidences. This can only be done if stakeholders share data from which the patterns and trends can be discerned.

Current efforts are directed at supporting President Biden’s “100-day plan” to shore up industrial control systems and operational technology (OT—the stuff that is inside your plant running things) by addressing global supply-chain vulnerabilities.

Among the factoids gleaned from Cancel’s presentation:

    • 43% of respondents to a recent survey said they were either “not confident in” or “not sure about” their company’s emergency response plan to address physical and cybersecurity threats.
    • Unpatched vulnerabilities are the cause of one-third of all breaches of Microsoft software.
    • There has been a 48% increase in vulnerabilities between 2019 and 2020.

Fortunately, most problems can be addressed by paying attention to the basics of strong password usage, endpoint management (centrally and remotely monitoring servers, PCs, mobile devices, etc) and secure remote access.

Industry aims for more accurate assessment of creep damage in high-temperature boiler, turbine components

By Team-CCJ | February 4, 2022 | 0 Comments

The High-temperature Defect Assessment conference has drawn international participation since its inception in April 1998. HIDA began as a European Commission and industry supported research project aimed at unifying defect-assessment procedures validated on materials of interest to high-temperature processes—primarily power generation.

HIDA continues to meet periodically in response to industry developments and with a strategic focal point. The first two events, in France and Germany, concentrated on the beginning and end of the original four-year European Commission program. HIDA-3, held in Lisbon, Portugal, focused on crack growth and repair of high-temperature welds.

HIDA-4, in the UK, saw an industry need to dive further into probabilistic assessment, and was followed by HIDA-5, again in the UK, to discuss fitness-for-service and risk-based inspection. Moving to Japan in 2013, HIDA-6 concentrated on martensitic steels and creep-fatigue interaction, followed by HIDA-7 (UK) discussing life and crack assessment for industrial components.

Like the first seven events, HIDA-8 was organized and coordinated by European Technology Development Ltd, Leatherhead, UK. Its focus: crack inspection and assessment, repair options, and monitoring of cracks and pre-crack damage. Participants represented Australia, Belgium, Germany, Ireland, Italy, Japan, the Netherlands, Poland, Spain, South Africa, Sweden, Switzerland, the UK, and the US.

Dr Ahmed Shibli, managing director of ETD, opened the virtual meeting, held April 20-22, 2021, by stressing the values and benefits of this ongoing, dynamic collaboration thusly:

“Assessment of the behavior of high-temperature plant components containing defects and operating under steady and/or cyclic load conditions has become an area of urgent need and interest. We have strategically organized HIDA-8 into sessions dedicated to inspection, damage, and cracking under creep, fatigue, and oxidizing conditions; defects/cracks and life assessment; and martensitic steels—cracking, life assessment, and modeling.”

Consulting Editor Steven C Stultz participated in HIDA-8 for CCJ ONsite and provided the following highlights from the more than 30 presentations and online discussions.

Casting weld defects have become a significant industry concern. Ronnie Scheepers, Eskom, South Africa, discussed acceptability assessments of casting weld defects under transient thermal loading. The basis of this presentation was weld repair of castings during both manufacture and operation, emphasizing the need for qualified welding procedures and strict quality control.

In many cases, cracking (on initial assessment) is attributed to in-service creep damage accumulation. However, consideration of specific geometry and operational stress distribution often suggest stress relief or reheat cracking because of an original manufacturing weld repair.

“Weld repair of castings during manufacture,” he stated, “is a well-known and acceptable practice if conducted in accordance with approved standards and procedures. However, cracking of these weld repairs in high-temperature and ageing plants, especially those operating beyond design life, is all too common.

“Structural-integrity assessments of such components must not only consider reduced material toughness caused by temper embrittlement, but also the stress intensities generated during transient thermal events, such as start/stops and quenching incidents,” he continued.

“Most defects are detected during outage inspections of in-service plants,” the speaker explained. “The focus then becomes a management strategy of replace, repair, excavate, or leave as-is.”

The first of two case studies presented by Scheepers discussed the acceptability of weld-repair defects in the outer casing of an HP turbine. This 1980s-vintage unit for a 618-MW site had logged 220,000 hours and 328 starts. Material of manufacture is GS17CrMoV5-11 (1.7706). Operating conditions are 4.3 MPa at 330C to 430C.

Phased-array NDT showed an internal defect about 48 mm deep in a wall of 114-mm thickness. An external vertical defect was about 78 mm deep where wall thickness (WT) was 108 mm; an external horizontal defect about 63 mm deep (108 mm WT). Refer to Fig 1. Remaining ligaments were clear of indications.

Microstructural evaluation showed a mixture of ferrite and mostly bainite, and confirmed cracks in both the weld and in the heat-affected zone. Cracks were oxide-filled with decarburization along crack lengths, and no indications of propagation.

Metallurgical assessments concluded significant temper embrittlement had occurred. This was considered in a finite-element-based structural-integrity assessment that reflected design operating conditions as well as a hypothetical quenching event.

A second case considered an LP-turbine bypass valve, 1980s vintage from a 686-MW unit with 190,000 hours and 155 starts (Fig 2). Operating conditions were 4 MPa/535C during startup and shutdown; the baseload operating temperature, 248C. Material: GS17CrMoV5-11.

A 67-mm-long surface-breaking defect was identified by magnetic-particle test (MT); phased-array ultrasonic testing (PAUT) indicated a depth of 44 mm within 65-mm wall thickness. No other defects were found. A macro crack in the weld repair area was oxide-filled and micro cracks were found with stress-relief voids.

Weld repair had not been reported during manufacture.

In this case, the material temper embrittlement was found to be less severe, but the criticality of pre-warming to reduce transient thermal stress and, by extension, crack stress intensities during trips or shutdowns, was clearly demonstrated.

Remaining life assessments, in both cases, considering creep or fatigue crack growth and allowable defect sizes concluded the defects to be acceptable for operation to the next planned outage.

Predicting creep damage. Rolf Sandström, Materials Science and Engineering, KTH Royal Institute of Technology, Stockholm, Sweden, provided a tutorial on creep damage.

During creep deformation, he explained, several changes in the microstructure occur that tend to reduce the time to rupture. These changes include cavitation, substructure coarsening, particle formation, particle coarsening, and recovery of hardening phases. These are often referred to collectively as creep damage.

“Information on creep damage is used to predict the remaining life of materials and components and to improve the properties of existing materials,” he said. “To make predictions, accurate data about the creep damage is essential. Since extrapolation to longer times is almost always involved, methods must be available to perform this. Considering the number of damage types, it is a challenging task.”

He then clarified: “In recent years, creep models based on physical principles have been developed that do not rely on the use of adjustable parameters. These models are referred to as fundamental.”

Such models, he explained, represent a major advantage, since damage types that have not been possible to measure precisely can be predicted. In this way, a more complete picture of the creep damage can be obtained.

For several materials, rupture is controlled primarily by cavitation—at least when the stresses are not too high. Fundamental methods have been formulated that can predict the observed strain dependence of creep cavitation.

Referring to published works, Sandström noted that a common way to determine the creep damage has been to analyze tertiary creep. Changes in the dislocation structure are the main cause of tertiary creep, so the mechanisms are different in comparison to those controlling the failure. However, the data from tertiary creep still give valuable insight. “Fundamental models for tertiary creep have only recently been developed,” he said.

Sandström demonstrated that by taking all the main damage mechanisms attributed to dislocations, particle formation, and cavitation into account, the rupture life of austenitic stainless steels has been predicted successfully.

Sandström’s presentation was designed to review recent modeling of creep damage using fundamental methods. “In all work on creep,” he stated, “it is important to identify the operating mechanisms. To generalize and extrapolate the results can only be done if the operating mechanisms are known.”

He reviewed several examples where mistakes have been made in applying empirical approaches, such as the following:

    • The stress exponent n is used as an adjustable parameter in many models, even in those that have a partially physical basis.
    • At the same time, the n value traditionally has been used to identify the creep mechanism.
    • This is problematic knowing that, for example, the creep exponent for dislocation creep can take values from 1 to 50.
    • It is documented that a stress exponent of 1 is not enough to identify the mechanism as diffusion creep.

Resolution, Sandström stated, is in the use of basic (fundamental) models where the derivation of the model is based entirely on physical principles and all parameters are well defined and their values are known. There are no adjustable parameters involved.

He reviewed several models fulfilling these requirements, including:

    • Models for dislocation creep covering low-to-high stresses.
    • Models for solid solution and precipitation hardening during creep.
    • Influence of prior cold work on creep life.
    • Models for primary and tertiary creep.
    • Initiation and growth of creep cavities.
    • Development of cell and sub-grain dislocation structures.

“These models have been established for some materials but not yet for a wide range,” he stated.

Sandström then listed and reviewed the basic models for predicting creep damage:

1. Particle formation, transformation and coarsening. Can be handled with commercial thermodynamic software such as Dictra, Prisma, and MatCalc.

2. Coarsening of substructure (important for 9Cr and 12Cr steels).

3. Initiation and growth of creep cavities.

4. Tertiary creep.

He went on to give specific examples.

“These models are predictable,” he stated, “and can be used for generalization and extrapolation.”

Single-crystal materials. Kurt Boschmans, ENGIE-Laborelec, Belgium, addressed evaluation of high-temperature creep degradation in single-crystal gas turbine materials through both conventional creep testing and small punch testing, comparing the methods.

In 2020, ENGIE performed a study to stretch the maintenance intervals of a gas turbine within its fleet by evaluating the condition of post-service turbine blades and vanes. In the framework of this study, the high-temperature creep properties of the materials were thoroughly evaluated.

“Historically,” said Boschmans, “this evaluation has been performed by conventional creep testing on airfoil and root materials, and by comparing the test results to the known properties of the superalloys in question.”

Boschmans then explained traditional comparisons of creep properties using a material-specific LMP (Larson-Miller Parameter) curve.

In the framework of the new and expanded data project, a comparison was made between the results of conventional creep testing (CCT) of sub-size creep samples and results of small punch testing (SPT). The goal was to evaluate whether or not SPT could replace CCT in cases where there is insufficient material available to extract an acceptable creep sample from the available hardware.

“Conventional creep testing,” he explained, “has a minimum size requirement: M5 sample with diameter of 3 mm to allow creep testing in air. Sample extraction thus becomes critical for first-stage blades, as well as for evaluating aeroderivative gas-turbine hardware, putting limits on the method.”

The option of using sub-size samples, he explained, is possible but expensive. SPT requires much less material (a 0.5-mm-thick disc-shaped sample), but at the time of this study:

    • No internal experience was available.
    • Registered exporter (REX) data on single-crystal superalloys (anisotropic material) was limited.
    • There were no known comparisons of both methods on the same turbine blade.

Several studies were reviewed indicating that a relationship (conventional versus small punch) appears valid for highly anisotropic materials such as single-crystal superalloy in certain conditions. A good LMP-curve correlation was reviewed.

“Results confirmed that the material properties at high temperatures are still corresponding to the requirements of new material, suggesting a stretching of the maintenance interval is possible for the specific blade studied.” However, this study is recent and microstructural evaluation of the test sample is ongoing (as of April 2021).

Conclusions:

1. Evaluation of high-temperature mechanical properties of the same turbine blade by means of CCT and SPT verified both the feasibility and accuracy of small punch testing, for which no internal experience was available on single-crystal superalloy materials.

2. Test results illustrate the SPT results show a good correlation with the CCT that was performed in parallel.

3. For superalloy materials where the extraction of creep test samples is not possible, the application of small punch testing can provide an economical alternative to sub-size creep testing.

Operation in creep conditions. Jerzy Trzeszczynzki of Pro Novum, Poland, discussed the conditional operation of boiler components working under creep conditions until replacement, using a large utility boiler as an example.

One of the more serious operational problems is thermal-fatigue damage detected on internal surfaces of pressure elements (steam coolers and superheaters), especially those working under creep conditions. “Such damages are practically irreparable,” he said, “especially during a planned outage. They typically require fabrication of new elements.”

Using the technology of digital twins, fracture mechanics, and remote diagnostics, Pro Novum has developed and implemented a methodology of conditional operation (until the element is replaced or the boiler is shut down) that allows supervision of the damage under the control of an appropriate software. “The system can simultaneously control the possible development of a dozen or so damages and assess the condition of the element online,” he explained.

The elements operating the longest in these test conditions have worked for two years. Ultrasonic testing during operation, and destructive tests after the disassembly of the elements, confirmed the possibility of computational monitoring of crack propagation with an accuracy sufficient for practical operational purposes.

Examples also were described for headers that received endoscopic examinations during a utility boiler renovation in 2018. Crack depth ranged from 2 to 10 mm.

These components work in creep conditions, but periodically are exposed to thermal fatigue and thermal shock because of water-injection and condensate events.

The program goal was to further assess damage through fracture mechanics and achieve a schedule for conditional operation. This would include monitoring of working conditions, and periodic assessment of the technical conditions.

Trzeszczynzki summed it up: “Component replacement time can be determined with acceptable accuracy by monitoring conditions of the initiation of new cracks and the propagation of the existing cracks using the online calculation method and by verifying the calculations with controlled endoscopic and ultrasonic tests.

Using data scatter. “There is a large amount of scatter in the creep properties of welded joints of the steels; however, the scatter is not considered in conventional remaining-life assessments of welded joints of in-service piping.” This was the presentation opening by Masatsugu Yaguchi, Materials Science Research Laboratory, Central Research Institute of Electric Power Industry (Criepi), Japan.

“Thus,” stated Yaguchi, “we have developed a new method of assessing the individual creep properties of welded portions of actual pipes.”

This presentation explained the assessment method and described the actual implementation for Grade 91 steel, as an example.

The premise: “Data scatter (heat-to-heat variations) has not been considered for remaining-life assessment. Test specimens are taken to conduct creep tests and to analyze the data, but there is no data for the actual component.”

In Japan, the common method of remaining-life assessment for materials is the 99% lower-limit curves for data obtained at various temperatures, on a typical stress versus time-to-rupture diagram.

The question remains: “Is the 99% lower limit, or minus-20% strength, really ‘the weakest?’  Also, materials used in creep tests do not cover all specification ranges of Grade 91 steels (Fig 3).”

“Therefore,” stated Yaguchi, “consideration of heat-to-heat variations is important.”

The institute’s program objectives: Propose a life-assessment method considering heat-to-heat variations, develop a database and elemental technologies for Grade 91 welded joints.

In the method described, the creep property of the welded joint is related to that of each base metal because the creep properties of welded joints strongly depend on the creep life properties of the corresponding base metals.

Microstructure analyses and small punch creep tests on samples cut from the base metals at the outer surface of pipes in service were conducted, and the results were compared with a material database to estimate the creep property of each base metal of the target pipe.

The precision of the remaining-life assessment of pipes is significantly improved using the developed method because it can consider variations of the creep properties of their materials, which are not considered in existing life-assessment methods. Then, the method was applied to the welded joints of the pipes in ultra-supercritical power stations during periodic inspections, and remaining lives of the components were estimated (Fig 4).

Research continues at the Central Research Institute of Electric Power Industry, Yokosuka, Japan.

Looking ahead. European Technology Development has been deeply involved in HIDA conferences for more than two decades and will continue to both participate in and organize future conferences. Cooperation and knowledge gained from these events are critical elements of ETD’s ongoing commitment to the global power industry.

Other examples of the consultancy’s involvement include a recently published study titled “Review of 9-12Cr Martensitic Steels for Pressure Vessels, Steam Piping and Tubing,” focusing on Grades 91 and 92.

The guidelines presented in this report are based on the experience of ETD Consulting, the reports and experience of its International P91 Users Group and ETD’s network of consultants, the experience of international industry in general, EPRI guidelines, and latest research findings. It can be a valuable resource to plant owners/operators for material quality control, fabrication/welding, inspection, monitoring and repair, and for understanding the incidents of cracking/failure and how to deal with these.

The guidelines are of greatest value to decision-makers at plant design firms, plant owner/operators, service providers and steel producers. For more information, contact enquiries@etd-consulting.com.

UPCOMING HRSG FORUM EVENTS

Improve NH3 distribution to reduce NOx and ammonia slip

By Team-CCJ | February 4, 2022 | 0 Comments

Bill Gretta, principal, SCR Solutions LLC, presented two case studies at a recent HRSG Forum virtual session, in which a unique field test method combined with sophisticated CFD analysis suggested modifications for improving distribution of ammonia through the SCR catalyst modules to improve NOx reduction and ammonia slip. Old units, and many new ones, are not equipped with a permanent NH3 sampling grid downstream of the SCR, and it’s costly to add, Gretta said.

He described a method that makes use of a flexible weighted probe with NOx and NH3 sensors which is lowered into the SCR inlet and exhaust gas flow fields from multiple ports on the roof (photo). Then EPA Test Method 320 is applied. Subsequent CFD analysis revealed the reasons for areas of high and low NH3 concentrations after the ammonia injection grid (AIG).

In the first case study, a 2 × 1 501F-powered combined cycle with close to 500-MW output, this approach resulted in removing and rebuilding the AIG, locating it three feet closer to the CO catalyst, and adding mixing baffles and plates to reduce the root mean square (RMS, an indication of the quality of distribution, the deviation from the average of many values) of ammonia-slip variance from 70% to 10%; additional tuning got it down to 6%. Buildup of ammonium bisulfate in zones of high ammonia slip decreased dramatically.

In the second case study, a 2 × 1 501D-powered combined cycle installed more than 25 years ago had to meet a lower emissions profile, so a dual-function catalyst was selected, but failed to meet the new standards. Analysis showed there was plenty of catalyst, so other system issues were at play.

Gretta and his team simulated 501D exhaust, sampled at 50 data points in a 5 × 10 array of SCR inlet and outlet locations with the weighted probe, and then did an inspection and CFD modeling when an RMS value of 19.3 indicated poor distribution. Causes of poor distribution and solutions were similar to those identified in the first case study.

Insights gleaned from the Q&A included the following:

    • In both case studies, AIG heavy support elements (which Gretta said probably would be found only in early SCRs) were getting in the way of flow; the replacement was designed to be self-supporting to eliminate the old support structures.
    • Rust and scale were blocking the AIG ports. The new AIG uses stainless steel instead of carbon-steel pipe and includes cleaning and vacuuming ports in each lance. Hole diameters also were increased and rearranged.

UPCOMING HRSG FORUM EVENTS

 

Steam-side oxides, poor NH3 distribution tackled during second virtual HRSG Forum

By Team-CCJ | February 4, 2022 | 0 Comments

During the HRSG Forum’s second monthly meeting, June 2, 2021, hosted by Bob Anderson and Barry Dooley, close to 130 owner/operator representatives from 34 countries (out of 219 total attendees), were enlightened on two vexing issues with HRSGs: (1) steam-side oxide growth and exfoliation (OGE) from superheater (SH) and reheater (RH) tubes, and (2) the use of computational fluid dynamics (CFD) and field testing to improve selective catalytic reduction (SCR) unit performance.

Judging from the number and quality of the questions for both presenters, these attendees weren’t just staring at their screens. You don’t want to miss listening to recordings of the presentations all available at HRSGforum.com. They are rich in detail with a methodical sequence of illustrations for truly understanding the problems, impacts, and solutions.

Barry Dooley, a senior associate at Structural Integrity Associates Inc, whose experience dates back decades to some of the early work done at the UK’s CEGB, Ontario Hydro, and EPRI on OGE, explained how SH and RH ferritic steels like T11, T22, T5, T9, T23, and T91 are susceptible to oxide growth on inner surfaces containing greater amounts of hematite versus magnetite, which can lead to exfoliation of particles under the right thermal stresses (Fig 1). The progression of formation for different alloys, from laminations in the oxide layer to cracks to exfoliation, is well depicted in the slides.

The varying alloy compositions—chromium and molybdenum contents specifically—help determine how fast deposits grow, and the risk of exfoliation. The specific environmental factors are saturated or superheated steam, gas-turbine exhaust temperatures from 1100F to 1150F, use of duct burners, and tube temperatures ranging up to 1200F.

The deposits themselves can lead to tubes operating at higher temperatures, resulting in an ever-increasing oxide growth rate. The exfoliated material causes erosion, plugging, and sticking in valves; erosion of downstream HP and IP steam-turbine inlet-valve and steam-path components; or simply collects in a header (Fig 2). Impacts tend to show up after many thousands of operating hours but of course are aggravated by deep unit cycling and starts/stops, once the oxide reaches the critical thickness for exfoliation. Dooley shows one HRSG case in which material began to exfoliate after only 24,000 operating hours.

Unfortunately, OGE cannot be controlled through steam/water chemistry changes. It’s not dependent on O2 concentrations, but instead on O2 partial pressure. The influence of film-forming substances in the chemistry is uncertain. Shot-peened 304H and S304H SH tube alloys will exhibit a Cr-rich layer along the surface which slows the rate of exfoliation. “It’s rare for them to exfoliate,” Dooley said.

Among the insights that emerged from the Q&A session:

    • No relationship has been developed among operating parameters (for example., total operating hours, number of starts, etc) and OGE to predict its onset before impacts occur.
    • Cycle modifications which increase gas-turbine exhaust temperature raise the risk of oxide growth.
    • UT analysis can detect oxide-scale thickness but only lab metallographic analysis can reveal the characteristics of the oxide layer critical to OGE.
    • Early theorists suspected that steam/water O2 levels contributed to hematite formation, but deeper research has proved this false.
    • Small additions to the alloy, like vanadium and tungsten, will alter iron-ion migration patterns.

UPCOMING HRSG FORUM EVENTS

 

Diaphragm dishing most severe in steam turbines installed during the last three decades

By Team-CCJ | February 4, 2022 | 0 Comments

The “Diaphragm Dishing Issues” presentation by Steampath Engineer Jeff Newton in MD&A’s Spring 2021 Webinar Series (February 18) addressed permanent axial distortion of steam-turbine diaphragms, commonly known as dishing. The effect is usually caused by deficiencies in main weld depths, weld materials, welding processes and/or steampath design with the maximum movement at the horizontal joint where the diaphragm is weakest, according to Newton.

Unless you are already an expert on steam-turbine condition, you’ll want to see the photos shown during the presentation to get a good sense of dishing (not to be confused with thermal distortion) indicators, including: outer-ring distortion, evidence of main structural weld failure, reduced axial clearance at inner setback face, rubbing, packing high teeth out of location, horizontal-joint gaps larger on the discharge side, and packing bore diameters larger on the discharge side.

If you think you have a weld failure, get a second opinion quickly; that will require immediate repair, says Newton.

Steam turbines of 1950s to mid-1960s vintage typically experience the worst dishing in the third reheat stage. That’s because it is the highest-temperature stage with carbon steel used as the seal weld material between the partitions and spacer bands, notes the steampath engineer. The condition is more prevalent after 40 years of operation; the expected design life of turbines from that vintage was 30 years. There also was a better pool of data because steam turbines underwent major inspections and outages every five or six years.

However, it is important to note none of the diaphragms from this time period actually failed, stresses Newton.

Things get dicier beginning in the 1990s. At least one manufacturer began to replace submerged arc welding in these areas with electron beam and MIG welding, which led to less consistency in weld quality; the CrMoV (chromium, molybdenum, vanadium) metallurgy was changed to just CrMo; dense-pack designs led to more stages with less axial space; and diaphragms were not as thick. Main weld depths as a percentage of partition axial height also were reduced. Furthermore, the time between major outages was extended to more than 10 years.

These units have experienced diaphragm failures (Fig 1). One Toshiba unit failed within five years at the first IP stage. In fact, the three examples Newton reviews are all Toshiba. A second unit also failed at the first IP stage; bucket and rotor material were found missing at disassembly.

Three of the ways to proceed if you have evidence of dishing are do nothing and monitor, install offset packing rings, and/or shift the diaphragm upstream with a steam seal face insert. However, Newton stresses, these do not address the cause of the dishing. The component has to be reconstructed, or reverse engineered with design changes to address the cause (Fig 2). Newton illustrates this for users with a photo montage sequence that drives home the as-found versus repair comparison.

European HRSG Forum shines spotlight on tube failures, cycle chemistry, materials issues

By Team-CCJ | February 4, 2022 | 0 Comments

Co-Chairs Barry Dooley of Structural Integrity and Bob Anderson of Competitive Power Resources hosted 90 participants from 17 countries at EHF2021, a virtual event conducted May 18 and 20. More than 60% of the attendees were from 15 generating companies.

The 18 presentations made during the meeting covered new information and technology related to HRSGs, plus case studies of plant experiences and solutions. Topical open-discussion sessions among users, equipment suppliers, and industry consultants were integrated into the program.

The mix of different topics (including materials chemistry, operation, valves, tube failures and assessment techniques, inspection, and cleaning) proved of great interest to attendees judging by the robust Q&A and discussion—thereby confirming the value of forums promoting the global exchange of technical information.

The European HRSG Forum is supported by the International Association for the Properties of Water and Steam (IAPWS) and is conducted in association with the Australasian Boiler and HRSG Users Group (ABHUG) and the US-based HRSG Forum with Bob Anderson. EHF2021 was sponsored by Trace Analysis and Swan Analytical Instruments and organized by PPChem AG.

Connect with EHF2021 Sponsors

Conference highlights

HRSG tube failures (HTF) remain a major concern, with these aspects among those discussed:

      • Flow-accelerated corrosion (FAC), with clarification of the effect of oxygen levels and the use of oxidizing treatments (no reducing agents) in addressing single-phase FAC.
      • The major features associated with creep and creep-fatigue. Note that, while HRSGs typically operate in both the cyclic mode, and for periods at relatively constant output, that does not mean failures can be attributed to creep-fatigue.
      • The importance of metallurgical analysis to identify/confirm the mechanism of failure was emphasized as the first important step in addressing HTF.
      • Several attendees attributed pressure-part failures in superheaters and reheaters to condensate, drains, and attemperators.

Updates on HRSG cycle chemistry from around the world included the following:

      • The latest chemistry-influenced reliability statistics, referred to as Repeat Cycle Chemistry Situations (RCCS), showed overall improvement for the first time in 10 years. For background, retrieve the special report, “Trends in HRSG reliability, a 10-year review,” published in CCJ No. 61 (2019), p 44.
      • An update on the application of film-forming substances (FFS)—both amine- (FFA) and non-amine- (FFP) based—reminded users that a significant reduction in the quantity of corrosion products can be achieved, but that tube failure problems and deposits (a/k/a “gunk”) can occur if the FFS is not applied with expert guidance.
      • Assessment tools and instruments for monitoring film-forming amines (FFA) using OLDA (oleyl propylenediamine) were introduced.
      • The latest IAPWS Technical Guidance Documents for combined-cycle/HRSG plants were reviewed.
      • A good example of optimal cycle chemistry for a dual-pressure HRSG was presented.

An overview of the problems associated with HP bypass-valve erosion by wet steam were highlighted based on a successful recent workshop held on the topic at the HRSG Forum. [link to the HRSG Forum panel recording] Information shared confirmed the need for plant designers to focus greater attention on providing for sufficient warming steam flow in the HP piping between the HPSG outlet and the isolation valve at the HP common manifold.

EHF2021 featured several presentations related to materials of construction and analysis. Points made included these:

      • There can be challenges associated with introducing creep-strength-enhanced ferritic (CSEF) steels in HRSGs, including T/P 91 and 92. Discussion included the relatively new “zinc effect,” which has caused cracking in welds where zinc-based paint was used to protect material prior to fabrication. A poll of EHF2021 users indicated only a small percentage of the attendees had knowledge of this application and failure/damage mechanism.
      • A compilation of different failure modes associated with welds, and the good (and bad) welding and repair practices used.
      • Advanced approaches to component fatigue evaluation.

The latest research and case studies on pressure-wave technology for fireside cleaning of HRSGs. Some discussion also focused on the possibility of internal oxide/deposit dislodgement.

Large sidewall casing penetration seals: The latest approaches applied to design and fabrication.

An update on drum-level instrumentation and regulatory requirements.

Introduction of new, retrofittable steam-cycle technologies—including modular once-through boilers rated less than 100 MW to accommodate flexible operation.

Scroll to Top