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Steam Turbine Users Group 2019: Vendor presentation recaps

By Team-CCJ | February 21, 2022 | 0 Comments

“Steam Turbine Repair Planning and Execution,” Bryan Grant, Advanced Turbine Support LLC.

Whether you inspect/repair your plant’s steam turbine or contract out those services, Bryan Grant’s presentation is a valuable reference for O&M personnel, one possibly worthwhile reviewing ahead of your ST inspection/maintenance outages. It’s available on the Power Users website 24/7.

Grant offers tips on repair planning, blade replacement, J-seal installation, when to repair/when to replace nozzles, and final inspections. Plus, he stresses the importance of final FME (foreign material exclusion) close-out inspections prior to unit closure.

One of the speaker’s messages: Be prepared, especially when finger dovetail replacements are involved. Some of the retention pins will hang up during removal, he explained, but most can be persuaded to come out with a hilte or peening gun. Those that remain often must be machined out. This can be a risky operation because it’s easy to damage dovetails.

Risk mitigation during finger dovetail installs demands close attention be paid to the availability of parts and reamers. This entails verifying the sizes of pin holes as designed and to be aware of any oversize holes identified during previous outages. Grant said the lead time for the all-important reamers is upwards of about two months. How many should you order? His rule of thumb is to restrict reamer use to 20 holes. When reinstalling pins, he continued, start at the bottom hole and work your way up.

J seals received significant air time. Not every turbine has them, and all J-seal designs are not the same, Grant went on. Inspections for straightness and crush checks were described. Make sure the J seals are installed correctly with respect to steam flow, he noted. If installed backwards the steam flow acts to pull out the seal. Remember, you want a small gap where the two hemispherical sections of the J straps meet. Photos in the slides show what to look for during J-strap inspections.

Regarding hardware inspections, Grant urged attendees to replace: Never reuse old hardware. Photos described the proper procedure for conducting balance-weight and L-0 mid-span inspections. Staking of balance weights was said to be “incredibly important” to assure weights do not escape during operation. Decisions on diaphragm repair versus replace also were illustrated by way of photos.

“Fluid Film Bearing Visualization,” Dr Lyle A Branagan, Pioneer Motor Bearing Co.

Lyle Branagan is a familiar face/voice at user-group meetings in person and online. His well-illustrated presentations typically cover the design basics of journal and thrust bearings for motors and gas and steam turbine/generators, materials, lubricants and lubrication systems, machine dynamics and performance, installation/operation/maintenance, the importance of quality control, etc.

If you’re new to the business of power generation, listening to or thumbing through the slides in one of Branagan’s presentations is a good way to get introduced to bearings. If you’ve been on the deck plates for several years and haven’t been exposed to bearing work recently, his PowerPoints and videos are a good refresher.

Branagan’s presentation before the 2019 STUG meeting is available in the Power Users library,  a video of his 2020 7F Users Group presentation can be accessed at Power Users and in CCJ’s webinar library. 

“Failure Modes for Hydraulic Components and Control-Valve Actuators for Steam- and Gas-Turbine Applications and Strategies to Mitigate,” Ralf Bentfeldt and Tom LaCombe, Rexroth, a Bosch company.

This is another presentation available on the Power Users website that you might want to link to for your personal library of troubleshooting best practices. Valve actuators typically are an afterthought until they suffer an operational hiccup or must be removed for inspection and maintenance. [link to article] That probably doesn’t happen more than once a year, so it can be difficult to remember everything you should.

The speakers mentioned that 70% of hydraulic-component replacements are attributed to surface degradation—from abrasive, erosive, adhesive, and fatigue wear—and that 71% of these causes of mechanical wear can be associated directly with hydraulic-fluid condition. That means they are within the user’s ability to monitor and control.

Common fluid issues impacting mechanical wear of hydraulic components are temperature and viscosity, water ingression, air entrainment/cavitation, and contamination. The presenters cover each of these mechanisms individually, offering best practices and rules of thumb to improve outcomes on the deck plates. Example: One chart that illustrates the impact of low viscosity on component wear and the optimal fluid temperature to minimize physical contact between internal parts.

“Benefits of an Alternative Material for In-situ Hardfacing of Valve Seats,” Joerg Schoepp, Power Service Group.

Cobalt chromium hardfacing alloys 6 and 21 have been used to overlay high-wear components—such as steam-turbine valve seats—for decades, protecting against oxidation, impact damage (valve closing), solid-particle erosion, and friction-related wear. Industry requirements that valves be fast-acting while operating at temperatures approaching 1100F in some plants are linked to delamination of the CoCr layer from the high-chrome (9% to 12%) base material. Liberated metal causes downstream damage to components in the steam path.

A buffer layer between the base material and hardfacing has worked in some cases, but it creates additional steps in manufacturing and refurbishment of valve seats, increasing both cost and time. Plus, some recent valve designs have the added complexity of seats that cannot be removed for refurbishment, dictating in-situ seat replacement. Several slides provide key steps for in-situ seat replacement (photos are included) and attest to the challenges of hardfacing in the field.

Joerg Schoepp speaks to the company’s positive experience in using a single layer of Inco 625 for valve seat protection. By eliminating the buffer layer, the company’s general manager of repair services says, “greatly reduces outage duration and variability” while also mitigating the risk of the hardfacing layer to liberate from the base material.

“Technical Considerations for Optimizing Steam Turbine Startups,” Matthew P Scoffone and Thomas R Reid, PE, TG Advisers Inc.

The consultants consider both vintage and modern steam turbines in their presentation. Regarding the former, they identify the following as possible impediments to faster starting for economic benefit: HP/IP creep and embrittlement concerns, solid particle erosion, rotor bow, and casing cracking; for the LP section, stress corrosion cracking and water-droplet erosion.

Modern and retrofit steam turbines are characterized by less accumulated fatigue damage, a more aggressive duty cycle (cycling service, for example), turbine inlet steam temperatures of 1050F and higher.

The presentation [link] offers insights on how vintage rotors age, the importance of correct hold speeds, pre-warm to reduce the mismatch of steam and metal temperatures, clearance considerations for cycling, and startup modifications.

The presenters assure that opportunities exist to safely reduce cold start times without capital upgrades. They are identified by use of recent inspection results, finite-element analysis, and modern fracture mechanics principles. In their experience, cold-start times on legacy turbines typically can be reduced by 25% to 50% while still adhering to critical OEM design parameters and requirements.

“Fundamentals of Steam-Turbine Valve Maintenance,” Mark A Cohen and Scott Cavendish, PE, Independent Turbine Consulting LLC.

Mark Cohen and Scott Cavendish dig into the details of steam-turbine valve maintenance, touching on valve sticking and oxide management, in-service monitoring of valves, extending maintenance intervals, balance-chamber failures, and valve actuators. The presentation is heavily illustrated with meaningful photos. For example, the photos of valve oxide and stuck valves were taken immediately after valve outages where the oxide was not properly removed and the valves had to be taken apart again to correct the failed attempt.

Cohen, a hands-on maintenance expert who probably has forgotten more than many have learned in their careers, is an engaging bareknuckle speaker who maintains your attention with a seemingly inexhaustible supply of anecdotal case histories. Thus, the formal presentation posted on the Power Users website doesn’t cover all that he shared at the meeting. If Cohen presents at the upcoming virtual 2020 STUG conference starting November 11 be sure to tune in.

Restoring design clearances to original dimensions was the first topic. The speakers said 80% of valve sticking incidents is traced to incorrect high-temperature oxide maintenance—such as not honing and using try-bar go/no-go checks. Attendees were warned that grit blasting does not remove oxide, it only polishes surfaces. Reason: Oxide deposits are harder than the grit. When asked about the proper valve maintenance interval, Cohen said it depends on the oxide growth rate. Scale, he continued, is like bark on a tree: It keeps growing until you remove it.

He stressed that oxide removal to bare metal is tough hand work typically using nominal 60-grit bricks; higher doesn’t work, Cohen assured. A couple more best practices shared:

    • Never change a part unless it really must be changed because you could make an error in replacement and make a good thing bad.
    • On bolting up valve connections, stud tightening must be done until you see sealant squeeze out. Leaks on 1960s machines that never existed previously, it was said, testify to today’s lax work procedures.
    • In-service operational monitoring can detect only stuck valve, not insufficient clearances caused by oxide buildup.

“Don’t Do That to My Steam Turbine” was the second part of the presentation by Cohen and Cavendish. It focused on operating procedures to avoid turbine damage, including the following:

    • Adhere to starting and loading temperature matching to minimize life expenditure and avoid cracked shells and distortion of hot parts. Remember that metallurgical life cannot be restored. Example: Cracked shells cannot be fully repaired back to new metallurgy, only temporarily patched. And when shells are patched it’s even more important to temperature-match.
    • Quenching during an improper shutdown causes the most damage; it puts metal surface in tension. During shutdowns, avoid low/no-load operation with a hot rotor. On a hot restart, avoid quenching hot parts.

An example of quenching damage to valve parts was presented. Boiler producing 1000F steam tripped with a resultant drop in steam temperature to 750F-800F. Inspection revealed cracking to three valve seats and stems. Keep in mind that the differential expansion of stellite is twice that of the base material.

Some podium time was dedicated to turbine layup and the corrosion damage and stress corrosion that can result if proper procedures are not followed. Avoid moisture entry into the casing and oxygen-induced corrosion with dehumidification, inert gas and sealed casings, heat, and covered storage, the group was told. Periodic rotor rotation and filming amines were among the suggested actions.

“Advanced Single-Layer Turbine Warming System Improves Startup Flexibility,” Pierre Ansmann and Norman Gagnon, ARNOLD Group.

Pierre Ansmann and Norm Gagnon opened their presentation on “the most advanced turbine insulation combined with a high-performance heating system to improve startup flexibility,” by summarizing its value proposition thusly:

    • Increased in-market availability.
    • Lower startup costs.
    • Reduced thermal fatigue and longer mean time to repair for critical components.
    • Increased operating flexibility.

The duo reviewed the different warming-system arrangements, rejecting those integrating the heating circuits in insulation blankets, installing the heater on a thin mattress below the blanket, and using gas-fiber-insulated heating cable. The optimal system for the upper casing, they said, is heater on metal mesh baffle (Fig 1), for the lower casing, permanent mounting of heating cable below the split line (Fig 2).

The ARNOLD system features interlocking high-performance blankets which conform perfectly to the turbine surface as shown in Fig 3. High-quality materials and manufacturing, and long-term high-temperature resistance, allow the company to guarantee reuse of its insulation system for 15 outages without a decrease in efficiency. The insulation system for a 330-MW GE steam turbine is on the first page, integrated with the STUG logo.

More than five-dozen thermocouples, strategically located on the turbine, ensure proper heating. Each of the 18 or so heating zones has t/cs installed on the heating wires to double check if the zone is responding correctly and at the specified temperature. Below every heating zone, multiple t/cs are mounted on the casing to confirm even heating of the turbine.

Ansmann and Gagnon say the ARNOLD warming system can maintain your turbine in a hot-start condition for at least four or five days after shutdown. No preheating of the turbine is required prior to a start within this time period, reducing startup fuel consumption and auxiliary power.

To learn more about ARNOLD’s control system and blanket design, plus, how company technicians would go about custom-designing an insulation system for your steamer, be sure to tune into their 60-minute presentation at the upcoming STUG 2020 Digital Conference on December 9.

Turbine valves: How to prevent an actuator failure from tripping your plant

By Team-CCJ | February 21, 2022 | 0 Comments

The value of user groups continues to grow in the electric power industry as the number of employees on the deck plates shrinks and personnel with deep experience retire.

The plant manager for a 2 × 1 J-class combined cycle under construction told the editors he had received more than 500 resumes in the last two months for about 20 hourly positions at the facility. Two-dozen employees is the total headcount planned. Given that most candidates are not familiar with this gas turbine—only a handful of J engines are operating worldwide and the US fleet leader had less than a year of service time in February 2018—training time likely will focus on the GT because it is the revenue resource. Certainly would make sense.

What about the other equipment? Who is the subject matter expert (SME) on steam-turbine valve actuators, for example? Anyone? Not likely. The editors picked this for illustrative purposes because their Rankine Cycle experience comes from the nuclear and coal-fired plants home to large, hydraulically actuated steam valves and big staffs with SMEs for virtually every piece of equipment.

Before the Steam Turbine Users Group was launched in 2013, the major gas-turbine users groups may have dedicated half a day to steamers. STUG enabled owner/operators to drill down on important steam-turbine (ST) topics, like actuators, that weren’t covered previously because of time constraints.

Actuator inspection and overhaul was on the agenda for STUG 2016 and then again in 2017. If you’re a neophyte and don’t understand why this subject would be discussed two years in a row, by the same company (MD&A), you ask someone on the steering committee.

Here’s what the editors were told by a committee member with decades of GE steamer experience: Back in the days of “big steam,” he said, GE, the dominant turbine supplier, made its own actuators, which might have run for 30 years with little or no maintenance. In the combined-cycle era, Bosch Rexroth AG has supplied the majority of actuators for large steam valves and those must be overhauled every five to eight years.

Some actuator designs have specific issues that require close attention. For example, Rexroth actuators for Toshiba steam turbines are very large and oriented horizontally creating wear points that might not be found in the vertically mounted actuators on GE machines.

In the mind of this committee member, at least, actuators for turbine valves may be the most important “forgotten” component in a steam plant. Many problems, he said, can be traced to water ingress and maintenance inexperience. At his company, in-service failures and numerous servo and solenoid issues that had occurred when station O&M personnel were charged with maintaining actuators in-house have been avoided by contracting the work to a specialty shop.

But, the turbine expert cautioned that there are no guarantees when it comes to actuator reliability. Inspection and soft-parts replacement, which typically are scheduled during steam-turbine minor inspections, are done at intervals of about five years—a long time given the wear and tear traced to today’s demanding cycling requirements.

Because you don’t know exactly what you’ll find when an actuator is dismantled for inspection, be sure the overhaul partner you select can assure the ready availability of parts—unless you have a back-up set of actuators, as some owners do. Scuttlebutt suggests that getting parts from Rexroth, a German company, can be challenging. However, most users are likely to agree that Rexroth has the best actuator on the market today for steam valves.

To learn more about what owner/operators can do to minimize actuator issues, the editors spoke with MD&A’s Anthony Catanese, an engineer on the front lines of the company’s Ohio overhaul shop and the SME invited to speak at STUG 2017.

Actuator performance and lifecycle are influenced most by the cleanliness of the hydraulic fluid and your ability to restrict water ingress, Catanese said. Varnish presents a double whammy: It can plug the 4- and 10-micron filters for the servos, the actuator’s “brain.” Plus, it can combine with oxidation products produced during the degradation of the hydraulic fluid to form rust and varnish that inhibits actuator operation and may reduce spring life.

Given the importance of actuators and how easy they can be to forget in the daily crush of plant activity, consider assigning responsibility for them to one person in the O&M department. There’s not that much to do except keep after the few recommended activities for relatively few valves—eight in the case of a GE D11, an integral part of the OEM’s 2 × 1 and 3 × 1 combined cycles. Those plants typically are equipped with two each stop, intercept, control, and reheat valves.

When scheduling D11 overhauls, Catanese notes that some customers have opted to inspect and refurbish two valves every year to level both cost and outage time on an annual basis. Most often only about a week or two of scheduled shop time is required for the basic “open/clean/close” process and replacement of soft parts for a full set of eight actuators. An incoming inspection report with shop recommendations is generated shortly after actuator receipt. Plant personnel are invited to verify the report’s findings, discuss the recommendations, and witness testing after work is complete.

Of course, the technician assigned responsibility for actuators should be looking at them periodically when out in the plant. One of the first signs of concern often is leakage out of the packing-gland telltale weep hole. If borescope examination of the spring reveals moisture or rust, maintenance should be scheduled soon.

Moisture causes rust which can cause broken springs which, in turn, score the shaft and promote increased leakage. Plus, moisture can accumulate and contribute to the failure of springs on vertically mounted actuators. As a stop-gap measure, consider removing a breather vent and using dry shop air to pressurize the actuator, thereby preventing water/steam accumulation in the spring can.

Given the problems with varnish and moisture ingress that can arise over an actuator’s lifetime, it makes sense to spend time at the design stage to select the optimal hydraulic fluid for the service. If problems arise in service, give thought to replacing the fluid with one better suited to your application.

Finally, when your actuators leave the shop, be sure they are properly crated for shipment and possible long-term storage and secured in an upright position.

Steam Turbine Users Group 2019: User presentation recaps

By Team-CCJ | February 21, 2022 | 0 Comments

The speaker making the first technical presentation at the 2019 meeting discussed damage to the first three stages (blades and diaphragms) of his steamer caused by what he termed “magnetite throw”—a way of describing solid-particle erosion. An attendee mentioned that strainers were added to bypass valves at his plant to protect the turbine against such damage but he couldn’t contribute operational information to testify to the efficacy of this approach.

Trying to get meaningful discussion going early, a member of the steering committee asked attendees: “What’s the correct way to test the emergency overspeed trip?” He said the OEM had over the years assisted in checking the functionality of the overspeed trip. Recently he had heard that GE was writing software into the Mark VI to confirm trip operability without physically shutting down the machine. No one offered a comment.

A participant representing a 2 × 1 combined cycle said one of his plant’s heat-recovery steam generators (HRSGs), on an all-volatile treatment program, was showing high silica readings—and they were increasing over time. An attendee suggested that drain valves might not be operating properly. The affected user was urged to post a question on the HRSG Forum on the Power Users website. That online forum is chaired by Bob Anderson, chairman of the leading user group serving HRSG owner/operators, the HRSG Forum with Bob Anderson.

Valve seat delamination. The session moved on to a user describing damage suffered by a 262-MW D11 turbine at a 2 × 1 F-class combined cycle because of seat delamination associated with HRSG steam valves. The clue that something was amiss: Following a routine valve test, operators recognized that throttle pressure had to be increased by 70 to 80 psi 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 steam turbine:

    • Repair now (reliability outage). This lowest-risk option would require extending the current outage by six weeks and would result in significant unbudgeted expenses. Plus, the potential for additional discovery could add to both the time and cost of the outage.

    • Run short and repair when new buckets arrive. This would permit increased time for planning the optimal outage. However, the recommendations by experts would include a reduction in steam pressure (reducing output by about 12 MW) and no cycling of the unit offline. Plus, there is a risk that unidentified cracks might propagate.

    • Run until the major maintenance outage planned for spring 2019. Essentially the same pros and cons of running short, except a higher likelihood of cracking and damage because of the longer time between the outages.

Recommendations made to station management was to run until the spring 2019 major and order new buckets and diaphragms from GE for the first four stages of the unit. Important, too, was to monitor the unit for noticeable changes in operation that would indicate additional damage. Also recommended was initiation of a fleet-wide program to inspect and replace similar stellited valve parts and assemblies.

L-0 experience. A user discussing the design, operation, and maintenance of late-model L-0 buckets suggested that plant personnel track blade condition and failure probability over time to answer questions posed by corporate financial staff regarding operational risk. He reported finding indications on six L-0 blades extending from 0.25 to 0.33 in. from the trailing edge. One bucket was found with a 1.25-in crack starting in an area impacted by erosion.

An EPRI presentation complementing this experience urged station personnel to identify and track locations of erosion and to identify the source of the water. The speaker said erosion is heavily impacted by the angle of droplets hitting the bucket. He added that liquid droplet erosion can be found on leading and trailing edges on last-stage blades while operating in normal and off-design conditions.

The speaker encouraged the development online monitoring and inspection tools to identify damage on rotating equipment and to track the progression of LSB erosion. It was said that plants operating baseload can avoid erosion problems by using titanium L-0 titanium blades.

The topic of operating intervals between minor and major steam-turbine inspections was brought before the group. One user said he had two turbines running 80k hours to majors but said this might not be a time-based function for at least some machines. Depending on how your turbine operates, he said, you might want to schedule inspections based on operating hours adjusted by a starts factor. One practical suggestion was to check steam-turbine valves during 32k gas-turbine majors.

More on valves. The steam-turbine main stop and control valve presentation by an offshore user is especially valuable for its thoroughly labeled design and construction drawings and notes on how the valves operate. This introductory material facilitates understanding of the valve problems discussed in the remainder of the presentation. Used alone, the design and construction slides could serve well as a lunch-and-learn presentation and/or as a pre-outage primer for those involved with steam-turbine valve inspections.

Valve problems discussed by the presenter included the following:

    • Valve sticking during operation/testing.

    • Control valve closes during test but opens again.

    • Stop valve closes during test but opens again.

    • Turbine rolls off turning gear when stop valve opens.

    • Stop valve over-travels during closing.

 Possible causes associated with the stated valve problems:

    • Oxidation buildup on the bushing/stem section.

    • Oxidation buildup on the balance-chamber section.

    • Valve internal damage.

    • Actuator issues.

Sticking problems with steam valves are mentioned frequently in STUG meetings. This user’s data indicate why: He said the number of times control valves did not close below 95% open while performing online daily testing numbered six during a calendar year for one of his turbines, nine for another, and 10 for the third.

He then illustrated by way of several photos the valve dismantling procedure typically used to gain access to address the cause of the sticking problem. For the valve shown, there was oxidation buildup on the balance-chamber section—between the outside surface of the control-valve and the balance chamber.

The measured clearance at one location was 1 mil, not even close to the design clearance of 19 mils. Clearances before and after cleaning were provided at seven points along the disc’s path from close to open and vice versa. Clearances after cleaning were 18 or 19 mils at each location.

The root-cause analysis provided an interesting result. Poor steam chemistry was an early suspect, but all documentation received from the laboratory indicated that steam quality was perfect. What many readers may not know, the presenter said, was that the 12-chrome material used by GE in its steam-turbine valves has a short oxidation life—typically two to three years.

And, as you might have suspected, valve tests were not being performed daily and the valve operated in the full-open position for months—against the OEM’s recommendation and a cause of a more rapid rate of oxide buildup than normal. Daily testing would have helped to break up/remove the oxide layer forming and keep the valve operating freely for a longer period.

Three short presentations with both user and supplier participation addressed various aspects of cyclic-operation effects on stop/bypass valves designed for baseload service. The valves discussed feature a wear-resistant stellite inlay on the stem. Historically they operated reliably (no stem failures) with maintenance intervals of 24k EOH (equivalent operating hours). Stems were replaced at that interval because of erosion in the inlay region and/or bending at the threaded end of the stem that engages the stop-valve (SV) bypass disc.

But the wear and tear contributed by the shift to intermediate/cyclic operation dictated a change from traditional thinking. As a first step, a high-temperature diffusion coating process was implemented to increase the resistance to SPE (solid particle erosion) of the valves, which were manufactured with stellite 6 weld inlay in the erosion region of the bypass disc skirt. The coating increased to 130 hours the service interval for SVBP valves.

Note that service hours here are calculated by adding the SV bypass pre-warm hours and SV bypass online hours. As a frame of reference, consider that in baseload operation the SVBP valves might accumulate about 60 service hours during a 24k EOH maintenance interval, but in cyclic operation, with more hours in full-arc mode (throttling on SVs rather than control valves), that number might increase four-fold.

Manufacturers have responded with upgraded valve designs to improve the resistance of main-steam turbine stop valves to SPE. These would increase maintenance inspection intervals beyond the 130 hours provided by the diffusion coating. A non-OEM supplier presented on its design, compatible with legacy system requirements, noting that a redesign does not eliminate the underlying problem—solid particles released in the boiler—rather it reduces the effect particles have on valve components.

The OEM also offers an improved erosion-resistant design for the D11 fleet of stop valves currently being inspected on an 18-month interval. The design modification, it was said, incorporates a 50-deg seat/disc angle and changes the internal steam flow characteristics to redirect the particles away from the valve stem during throttling and high steam-flow velocities. In the design described, erosion occurs on the valve pressure-seal head assembly, which is hardened and reportedly erosion tolerant.

Given the recent valve developments, the presenter said his company has two cost options to consider:

First, it can perform stop-valve maintenance with outages at 130 SVBP service hours and replace steam-valve wear parts without inspecting the control, reheat, or intercept valves. At the following interval, the valve outage would include maintenance on the steam, control, reheat, and intercept valves. This would involve purchasing a set of spare stop-valve subassemblies and rotating of the spare assemblies into stock as repairable items. The repair of spare SV subassemblies would be done on straight time during off-peak shop hours.

Second, retrofit the stop valves with an improved design that would allow longer maintenance intervals and return to a traditional maintenance cycle with all valves inspected and repaired. Note that the second option eliminates the stop-valve-only outage required by the first option.

“D11 Main-Steam Lead Piping Cracks” is a timeless presentation that all O&M personnel should consider reviewing. The detailed case history begins, as you probably would expect, with deck-plates personnel noticing a small steam leak—in this case, in the HRSG steam supply line at the tee where it splits to go to the turbine’s two main-steam stop valves.

The steamer was taken out of service, insulation removed, and the pipe inspected visually. Cracks were found at the tee-to-reducer weld on one side of the pipe. The 12 × 14 reducer was removed. Then the tee, and the piping on the turbine side of the reducer, were checked visually. Of course more cracks were found: How often do you find only one?

A crack was discovered on the inner wall of the tee at the horizontal-to-vertical transition. It was ground out and a penetrant inspection confirmed it had been removed. While NDE technicians were onsite, PT was conducted at the bottom of the tee, at the low-point drain junction. More cracks were found there. The still more cracks were found in the exposed sections of the steam piping. The result: The tee and 12 × 14 reducers on either side of it were replaced. Still more cracks were found later in several welds, including a couple of through-wall cracks.

An engineering review of system history was conducted. The piping had been exposed to approximately 730 startup/shutdown thermal cycles since COD, plus nearly a thousand transitions from 2 × 1 to 1 × 1—likely more severe transients than designers would have expected.

No PM records having being found, investigators concluded that inspections of main-steam-system welds had not been conducted after plant construction—perhaps because historical industry experience suggested this was a low-risk system. They also concluded that the root cause of the cracking was water intrusion.

Supporting this conclusion was that the steam-seal spray-water control valve and associated automated blocking valve had suffered erosion damage and/or seat degradation. This was already known and the unit was operating with the steam-seal spray-water manual isolation valve closed until an outage opportunity.

The leaking valve allowed water to enter the main-steam piping. During normal operation, the leak-by would have flowed to the steam-seal header, where drains removed it from the system. Erosion across the steam-seal spray control-valve seat likely was the result of excessive cycling. The seat was replaced.

The RCA investigation dug into the details, confirming that the cause of cracking in the main-steam system was thermal fatigue crated by cool water inadvertently entering the pipe while the unit was online or shortly after shutdown. Leaking valves in the steam-seal spray-water system were the source of the water. The investigation also determined that valve operating logic, the PM strategy for the valves, and startup procedures/testing for leaks all required improvement.

Engineers then set about creating a list of action items, as suggested by the RCA, to prevent a recurrence of the problems identified. The list included the following:

    • Install skin-temperature thermocouples at select locations and collect real-time operational data to support ongoing analysis.

    • Obtain additional samples from the full circumference of failed pipe to support additional analysis. Also, try to date the failure using the oxide layer.

    • Evaluate the current PM strategy for high-energy piping systems, giving consideration to reducing inspection intervals and expanding the inspection boundaries.

    • Some of the actions taken to date include these:

    • During minor and major steam-turbine outages, a robotic inspection of the main-steam piping adjacent to the valves will be performed.

    • An annual PM will be conducted on the steam-seal attemperator valve to check for leak-by.

    • Other units in the company’s fleet will be inspected similarly. Thus far, some cracks were discovered on another unit at the same site.

Finally, the experts believe cracking initiated about seven years before the steam leak was noticed by deck-plates personnel. A similar experience at another plant was reported earlier in CCJ.

“Lessons Learned to Shorten a Steam Turbine Major and Valve Outage,” has value to most, if not all, plant and headquarters personnel assigned to ST outage planning—especially those who haven’t been involved in this exercise previously. It is based on one owner/operator’s experience, so all points made might not apply to your specific situation.

It begins by suggesting both the responsibilities of personnel managing the outage, and the progress reviews and discussions among the parties that should be conducted, to ensure success. Next comes a slide on how/why to perform a steam-plant audit, which focuses on performance losses—recoverable and unrecoverable—attributed to both the thermal and structural condition to the steam path. The audit enables informed decision-making on components/parts that should be repaired or purchased new.

The speaker said that another benefit of collecting data for the steam-path audit is identifying the actual rotor location within the stationary components. This information may prove invaluable later if realignment is necessary.

Other lessons learned/best practices that you might find useful include these:

    • If your steamer is a D-11, purchase or repair decisions will be required for dished diaphragms. Suggestion is to purchase ahead of the outage new diaphragms for stages identified with a high risk of dishing (one to five and 12 to 16 in the case presented) and send the dished ones removed to a third-party vendor for restoration and use in a sister unit.

    • Consider using a third-party vendor to supply and install packing and spill strips, and to do laser alignment. For the seal work, a contractor with a portable machine shop to support field fit-up activities might be your optimal choice.

    • Arrange for turbine-deck storage racks and onsite machining to support diaphragm activities. The storage racks optimize floor space and minimize the use of a crane to move diaphragms between the time they’re pulled out of the machine and reinstalled.

    • Install a temporary freight elevator outside the steam-turbine building if one is not available inside and crane access is limited.

    • Consider not flipping over the HP shell and performing necessary repairs with the casing top side up.

    • Shorten your steam-turbine valve outage by having spare valve assemblies onsite. So doing, this user reduced valve outage time from a typical 14 to 21 days to five to 10 days. Spare assemblies help reduce your valve parts inventory as well as the cost of inspection and repair of valve assemblies because they are done off-peak.

If there are budget concerns, the speaker suggested a low-cost option for a spare control valve consisting of just the stem and disc; for a spare main-steam stop valve, just the stem, disc, and pressure-seal head. Several drawings and photos presented in the PowerPoint provide details.

    • Valve seat: Buy new or lap? For those opting for the latter, recommendations were given for lapping tools.

    • Final advice: Try bars are important.

There are several more user presentations from the 2019 STUG meeting that you can access in the Power Users library, including the following case histories:

    • HP-turbine blade liberation.

    • Failure of a main-steam control valve to shut on a turbine trip.

    • KN steam-turbine fleet issues.

    • Asset preservation program using data analytics to drive steam-turbine maintenance.

    • Lessons learned during a D11 minor outage.

    • Lessons learned during the major overhaul of a 416-MW GE D8 steamer (LP section) and valve inspection.

“Ask an Engineer”—an open forum. This was one of several discussion sessions strategically integrated into the agenda to provide attendees feedback on topics of interest.

There was a great deal of discussion on valves throughout the meeting. In one exchange, the topic of fine-mesh stop-valve strainer baskets was brought before the group. Several users suggested their installation ahead of work planned on the steam path from the boiler outward. They will collect grinding/welding debris. But don’t forget to remove the baskets before the unit is returned to service: They can plug over time, collapse, and go through the machine.

Strainer basket rotation was cited as another problem. The group was reminded that there is a pin for correctly positioning the basket. However, several incidents of pins snapping off because of negligent work practices.

A best practice for seat inspection on a combined control/stop valve: Don’t use a penetrant because you won’t see a crack when the valve is hot.

A user recommended conducting actuator outages every six years or at every other valve outage. At his plant, actuators are removed, crated, transported to the selected shop, overhauled, and returned. Dig deeper into the topic.

Another participant opted to forego a major on his KN steamer at 120,000 hours because several colleagues said their units did not work properly after their majors.

GUG 2019 Vendor Presentation Recaps

By Team-CCJ | February 21, 2022 | 0 Comments

What follows are abstracts of presentations and key points made by suppliers from the 2019 meeting—timeless content not covered previously by CCJ online or in print. The information shared here should help you decide to participate in the 2020 virtual meeting—it takes little effort, costs nothing, and you can learn so much.

To dig deeper on the topics that follow, access speaker PowerPoints on the Power Users website, which are available to registered owner/operators only. If you don’t already have a “library card,” register today. It takes only a few minutes.

“Generator Inspection Outages—Contingency Planning,” Jamie Clark, AGT Services.

Jamie Clark’s message was simple: Increased cycling of ageing gas-turbine (GT) assets, both simple cycle and combined cycle, is causing problems for owner/operators. The proof: Service providers say as much as 60% of their shop effort during outages is emergent work. “We’re running older units harder than ever,” he continued, “harder than they were ever designed to run.”

The speaker recommended that attendees follow the latest guidelines regarding periodic inspections. These have changed recently, he said. One example: The most recent OEM guidance has no reference to field removal unless prior robotic inspections dictates via findings, or operational events—such as motoring, sync out of phase, generator trips, etc—warrant.

He also suggested users do the following before the outage:

    • Take flux-probe readings.
    • Do EMI testing (refer back to the third item in the section above on user presentations).
    • Conduct partial-discharge testing.
    • Review reports from, and since, the previous outage to review what was not done as recommended.

Clark next discussed the pros and cons of robotic inspection. At the top of the “pro” list is that robotic inspection avoids the cost and risk of field removal/reinstall. However, findings from that inspection might suggest field removal, in which case you pay twice unless it’s possible to postpone work until the next outage.

The speaker called attention to the fact that robotic inspection equipment is a limited resource, especially with competent operators and generator specialists guiding the work. He suggested releasing robotic-inspection RFPs at least six months prior to the outage and ensuring service-provider commitments are in hand within three months of outage start.

Clark then reviewed reasons for pulling the field and explained work that can be done with the field in. The latter seemed particularly helpful to attendees. Here’s what he said regarding the stator: Minor endwinding repairs (tightening, partial-discharge damage, for example) are possible, as is belly-band tightening and possibly even core tightening—provided EL CID validation is possible.

Concerning the field, collector-ring grinding and replacement typically are possible, along with brush-rigging repairs and upgrades. Retaining-ring NDE also can be done, in addition to a few other tasks.

If it becomes necessary to pull the field, Clark reminded, be sure the proper tooling is accessible—including coupling/journal shoes, skid pan, body shoe, slings, turnbuckles, and rigging from stator ends. Don’t overlook the benefits of field extraction platforms—for 7FH2s in particular, and possibly AeroPacs. This is not “incidental equipment, requiring possibly two 53-ft tractor trailers. Cranes are another consideration: A 7FH2 field weighs more than 75,000 lb, a GE 324 field about 50 tons. How close can the crane you need get into your unit? Access is almost always an issue.

Clark continued, “So now your field is out and you’ll be shipping it offsite, what do you need to know?” Come up to speed on permitting procedures and details. Figure it will take a couple of weeks to get a permit and line up trucking for the optimal route. Be aware of the permit time required and on-road time, the speaker said, advising that it’s rarely a good idea for an owner to manage shipping.

Doing field repairs? Figure seven to 10 days minimum, 30 days maximum for these typical repairs:

    • Main-lead repair usually requires a No. 1 coil (both poles)—a partial rewind. But keep in mind that if you opt for this plan, the remainder of the field is “old.”
    • Crossover repairs may require a full rewind.
    • Slot armor delamination requires a full rewind.
    • Turn shorts usually indicate a global condition: Rewind.

An exchange field might be the best course of action if operating commitments are firm. Keep in mind, the speaker said, that while all 7FH2s and 324s are the same mechanically, they can be different electrically—for example, in numbers of coils and turns per coil, etc. A few points to remember: Only accept an exchange with current high-speed balance and at-speed flux probe data, no turn shorts, high-quality vibration data, and assurance of interchangeability.

If field removal is in your plan, think about what stator repairs are prudent. Clark concludes his presentation with recommendations for rewedging, repairs to endwindings and connection rings, and a complete stator rewind. The last typically takes between 20 and 35 days, but may go to 12 weeks if bars must be replaced and they’re not available off the shelf.

“Rotor Turn Insulation Failure,” Tyler Foutz, EthosEnergy Group.

Tyler Foutz’ short presentation concerned a rotor with 22k hours of run time that was exhibiting intermittent vibrations and flux-probe data discrepancies. Turn shorts were suspected and confirmed. The retaining rings were removed and endwindings inspected. Decision was to rewind. A root-cause analysis confirmed insulation failure and side-wall interference. Repair quality was confirmed by high-speed balance/flux probe.

“What You Need to Know About the New IEEE Standard to Extend the Life of Your Existing Electrical Bus System,” Steve Powell, EBI-Electrical Builders.

Steve Powell, known to users for his insightful presentations at annual meetings, reviewed the design, construction, testing, and performance of bus systems, as established by IEEE C37.23-2015 for metal-enclosed gear. He covered voltage ratings, rated insulation levels, continuous current, rated short-circuit and momentary withstand current, short-time withstand current, and temperature limits.

Powell reminded users that isolated phase bus systems have no backup and if a failure occurs, the plant will be offline until the bus is repaired. He urged attendees to follow the OEM’s recommended service schedule (annually during a normal shutdown or every 18 months) and to confirm what you think you see (or don’t) with EMI testing and thermal imaging. He also discussed the value of periodic offline inspection and cleaning.

“Modification of a Westinghouse Stator from Diamond Coil to Bar Design,” Andrew Adam, PE, EthosEnergy Group, and Caleb Munholand, The High-Voltage Coil Manufacturing Co.

The RFQ for a generator stator rewind stated no changes would be allowed to the nominal 54-MVA (13.8 kV) three-decades-old design except for insulation class (B to F). This stator was one of the largest diamond coils ever manufactured and the OEM and only one vendor still made the component. EEG, currently the OEM for legacy Westinghouse gas turbines and generators with access to original design prints and parameters, was the successful bidder.

EthosEnergy faced manufacturing challenges, as described in the presentation, motivating conversion to a Roebel bar design; design and manufacturing details are summarized in the slides. Because overall performance and output of the generator is largely dictated by the field, the speakers said, overall generator capability remained essentially unchanged. The new winding has the same number of turns as the original, resides in the same core iron, has the same amount of copper (or more), and has equivalent losses.

The stated advantages associated with specifying the three-turn Roebel bar design over the three-turn diamond coil are these:

    • Elimination of top-strand heating. Temperatures within the winding are evenly distributed because of roebeling.
    • Elimination of installation issues associated with the diamond-coil design mitigates significant user schedule and performance risks.

“Fiber Optic Generator Monitoring,” Derek Hooper and George P Dailey, PE, BPhase Inc.

Better techniques and instrumentation for monitoring the performance powerplant equipment are always welcome. The presenters focus on the use of fiber optics for reducing the risk of generator in-service issues caused by high core temperatures and loose wedges. The presentation includes many slides on development history for those interested in how the technology has evolved.

The stated value of the BPhase developments is the following:

    • The core monitoring system can detect any excursion from normal core operating conditions. The data allows plant personnel to see a core thermal event in progress, enabling a controlled shutdown before serious damage occurs.
    • The wedge tightness analysis system allows maintenance personnel to follow the degradation of the wedge package over time, enabling the planning of rewedging without need for disassembly or robotic inspection. This can predict coil wear through mechanical vibration and core damage through slot pounding—as the condition will be detected before significant damage can occur.

While acknowledging that fiber-based systems cannot perform visual inspections, the presenters say they can certainly reduce operational risk from wedge tightness and core-related issues, thereby reducing overall risk during extended operation as necessary.

“Generator Degassing and Purging: Best Practices for Safe Plant Operation,” Christopher Breslin, Environment One Corp.

Hydrogen is explosive, colorless, and odorless, as well as difficult to contain. Yet it has been used widely as a generator coolant since the late 1930s because its windage/frictional losses are less than for air and it has excellent heat-transfer characteristics.

It is essential for plant personnel to know and understand the hazards associated with hydrogen and that all equipment for handling and storing this gas must be certified and maintained in top condition. Finally, because purging is an inherently complicated exercise, and can be dangerous if performed improperly, all personnel involved must be well trained, non-sparking tools must be used, carbon dioxide must be readily available in sufficient quantity, appropriate safety signage must be in evidence in critical areas, and keyed lockouts must be provided for “air” and “hydrogen.”

Chris Breslin, known by users for his practical and valuable presentations, reviews primary elements of the hydrogen auxiliary system, including useful one-line diagrams, provides guidelines for the purging process and best practices for safe plant operation, and reviews requirements/considerations for automated de-gassing. Consider the presentation for a lunch-and-learn session in the plant conference room.

“Comparison of Low- and High-Frequency Partial-Discharge Measurements on Rotating-Machine Stator Windings,” G C Stone and H G Sedding, Iris Power (Canada).

The speakers are among the industry’s top experts in the partial-discharge (PD) testing of electrical equipment. They draw the following conclusions in their relatively short but informative presentation: Low- and very-high-frequency PD detection methods in machines each have very different advantages. For offline applications, it is clear that low-frequency testing is preferred because PD can be better detected regardless of where it occurs in the winding.

For online testing, of transformers for example, the very-high and ultra-high methods are preferred by users because the risk of false indications caused by noise is lower; therefore, test credibility is higher.

“Realities of Global Vacuum Pressure Impregnated (GVPI) Impregnated Generator Stator Repair and Rewind,” W Howard Moudy, NEC-National Electric Coil.

Howard Moudy may have made more presentations at user-group meetings in the last decade than anyone else—in the process covering all types of generator failures and their fixes. At the 2019 GUG conference his topic was the repair and rewinding of a GVPI stator for a 13-yr-old, 100-MVA, air-cooled generator serving a geothermal plant in Indonesia. The unit tripped with damage to the winding and core. Contributors to the failure as determined by a root-cause-analysis investigation included the following:

    • Endwinding vibration/resonance.
    • Core looseness/hot spots.
    • Key-bar deterioration at the core exit—ground-wall fretting and thermal deterioration, and strand fatigue.
    • Vibration transmitted from the phase-ring assembly.

The owner expressed preference for mechanical removal of the winding despite NEC’s deep experience with the generally preferred water-blasting process. Contract was awarded to a local company with NEC in an oversight role. The local firm did not have appropriate tooling for the job which NEC supplied later to enable job completion. However, other findings created uncertainties in the customer’s mind that led to replacing the entire core. A couple of dozen photos describe the work.

NEC came away from the project with the confidence in its ability to rapidly rewind/rebuild air-cooled GVPI stators anywhere in the world. In this case the time to manufacture a new stator winding and ship it to Indonesia was 38 days.

In his concluding remarks, Moudy acknowledged that the initial cost of GVPI generators is attractive but that there are maintenance concerns and limitations associated with a decision to go with GVPI. Finally, he said that with proper engineering and planning, GVPI generators can be rewound effectively to a coil VPI design that is more easily maintained and conducive to long-term reliable operation.

GUG 2019 User Presentation Recaps

By Team-CCJ | February 21, 2022 | 0 Comments

What follows are abstracts of presentations and key points made by users from the 2019 meeting—timeless content not covered previously by CCJ online or in print. The information shared here should help you decide to participate in the 2020 virtual meeting—it takes little effort, costs nothing, and you can learn so much.

To dig deeper on the topics that follow, access speaker PowerPoints on the Power Users website, which are available to registered owner/operators only. If you don’t already have a “library card,” register today. It takes only a few minutes.

Replacement of bushings. The focus of presentations by owner/operators was near equally divided among stators, rotors, and inspection/testing/general. One concerned the replacement of bushings on a nominal 265-MW (1980 COD) hydrogen-cooled generator that runs only four to five months annually at baseload. The well-illustrated presentation covers testing and repairs conducted to enable decision-making, issues faced during replacement (confined space, terminal plate bonded to the bushing plate, etc), and challenges post replacement—including the loss of hydrogen and a blown isophase connection.

Stator, rotor rewinds. The same user also presented on the rewind of both rotor and stator on a 65-MVA, 13.8-kV generator. Periodic maintenance testing revealed a high dc leakage value (120 microamps leakage at 1.25 times the dc value) and a winding resistance unbalance of more than 5%. Plus, rotor inspection revealed shorted turns and loose blocking.

During the rewind, one of the contractor’s staff got a drop of glue in his eye and the use of goggles was made mandatory. After the rewind, the endwinding was re-blocked. Return to service was not smooth, the unit tripping within one second after start attempts. The gremlin: The shorting cable installed on the CT circuit was not removed after generator testing.

Then issues surfaced in the excitation system. Personnel found one diode wired incorrectly on the rotating diode bridge. It took three days to rewire the diode bridge.

EMI testing. A hot topic in generator circles continues to be electromagnetic interference (EMI) testing to detect failing electrical connections—in particular, those inside generators and bus systems. Two significant presentations were made on the topic at the 2019 GUG meeting, with the dialog continuing at the 2020 conference beginning next week.

EMI has been used since the 1950s, possibly earlier, to locate defects in power lines that cause radio and TV interference. Application to powerplant equipment began in about 1980, motivated by the work of several Westinghouse engineers who found that energy discharges in electrical equipment—such as arcing and partial discharge—produce a broadband high-frequency emission pattern. The radio-frequency (RF) currents produced, the engineers said, flow in the machine neutral connection with a magnitude and spectrum signature that can be recognized and differentiated from other RF signals which may be present.

“EMSA [electromagnetic signature analysis] Training,” the first of the EMI presentations last year, is highly recommended by the editors for the background it provides. A significant portion of the presentation is devoted to work done since 2015 by National Instrument and a major utility to develop an affordable instrument for “continuous” monitoring of EMI in generators and transformers.

Fast forward to today, the utility has installed the instrument developed on more than 80 generators and 120 transformers in its fleet. A full-spectrum reading, taken about every 15 minutes, produces data for trending.

The presentation is particularly valuable for what the utility has learned over the years. Here’s a summary of that experience across the four frequency bands of primary interest:

    • 30 to 500 kHz. In this region, diode and SCR/Thrystor firing patterns are seen and the following issues can be identified, among others: dirt contamination on diodes, SCRs, and Thyristors; loose excitation cables/connections; missing SCR firing patterns, etc.
    • 500 kHz-5 MHz is where issues in the core slots of motor and generator windings likely would be identified—including loose wedges, slot discharge, and back-of-the-core arcing.
    • 5 to 30 MHz. Issues associated with motor or generator endwinding structure are likely identified in this frequency band—including loose winding basket, corona in the endwindings, broken strands, etc.
    • 30 to 100 MHz. In this frequency band, issues associated with the generator output bus and isolated-phase bus generally are found. Look for cracked insulators, insulator contamination, water intrusion, etc.

Another resource on the subject is the CCJ article “Simple EMI Test Detects Failing Joints, Promotes High Plant Availability,” by Consultants Clyde V Maughan and James E Timperley. You can access it by using the search function on the CCJ home page at www.ccj-online.com.

The second presentation last year on electromagnetic interference, “EMSA and IPB,” is a case history spanning several years that probably would be of interest to anyone having had to deal with moisture and other issues associated with isophase bus (IPB). In the end, EMI testing confirmed the generator was not the source of the problem as suspected by most “experts”; rather, it was a defective through bushing from the IPB to the B-phase potential transformer.

Field vibration, thermal sensitivity. One user presented several case histories, each with one or more detailed graphs of meaningful operating data and several highly instructive photos. The first case of an instantaneous increase in generator field vibration was caused by loss of mass. A step change in vibration was noted during a routine startup of the gas-turbine driver. Amplitudes were acceptable to allow the unit to remain in service until a planned shutdown about two days later.

Investigators found a liberated fan blade and stator winding damage when the generator was opened for inspection. The root cause: Improper installation of the bolt locking tab on the affected fan blade.

A second case history presented by the same user also concerned the liberation of a fan blade—this time in the generator coupled to the steam turbine. Once again, the unit was allowed to remain in service following the step change in vibration until a planned shutdown, this time in four hours. Inspection revealed a liberated fan blade and stator winding damage, plus many other bolts well below the design torque value. The root cause was high bending stresses on the bolt which led to fatigue cracking. Note that the fan was designed with a single bolt per blade.

A change in mass distribution caused a step increase in vibration (typically about 2 mils) on yetanother generator, but here it was because one of the retaining rings was pushed off-center by the copper winding under certain operating conditions. This has occurred periodically for many years. Correction: Bring the unit to turning gear, then back to speed to reset the retaining ring in the proper position.

Thermally induced vibration attributed to end-turn blocking was experienced by a large 2-pole field with eight coils per pole. Root cause: Blocking between the No. 8 coil and centering ring rotated out of position during installation. At high field current, the vibration increased by 1 to 3 mils and was not consistent in behavior. Multiple compensation balance-shot attempts were made over a five-year run.

Thermally induced vibration attributed to copper binding in slots was the subject of still another case history. Investigators found copper yielding in the slot exit area of three coils exceeded the design clearance in the slot. Looking at the generator’s operating history, engineers found the unit had experienced full-load rejection (FLR) a couple of times during the tuning of a new control system.

They believed that over-speed during the FLRs caused the position of the copper to shift relative to existing worn grooves in the slot liners. Copper expansion was limited and vibration increased/decreased proportional to field current. The field was rewound and the affected copper turns replaced.

Accidental energization. Your generator is designed to guard against inadvertent energization, but owner/operators should be aware unusual conditions that bypass the protection scheme for your machine can occur. And even with protection in place, the speaker said, there is no certainty that an inadvertent energization event will not cause at least minor damage. He noted that energization even for a few cycles is conducive to high current flow and possible arcing.

This introduction to the subject should provide the incentive to read on.

First the background: Accidental energization occurs when 3-phase voltage is suddenly applied to the generator terminals. Such an event is classified as “severe” when the rotor is at standstill or on turning gear.

What happens upon energization is that a rotating flux at synchronous frequency is introduced into the field. High-amplitude currents, similar to negative-sequence currents, circulate in the rotor. The generator behaves like an induction motor and the rotor attempts to accelerate. The result is rapid and excessive heating, particularly at locations of high current density and/or high-resistance connections—such as wedge-to-wedge and retaining-ring interference fits. Damage typically is associated with the rotor forging and rotor components, not the field winding, stator core, and stator winding.

Industry experience, the speaker continued, suggests that inadvertent energization events that are cleared quickly—within one second—will cause minimal damage—possibly no damage at all. However, events longer than a second are almost certain to cause damage, severe damage if the event is more than a few seconds in duration.

The case history presented, supported with many high-resolution photos, describes an inadvertent energization event that occurred when the subject 224-MVA, 20-kV generator (COD 1958) was on turning gear. The machine has a field winding with eight coils per pole and is of the tight-fit wedge design. The field had been rewound in 2003.

The details: A disconnect switch was closed onto a live bus and the stator winding was immediately energized; the normal protection scheme was bypassed. The rotor attempted to accelerate and instrumentation revealed that a speed of 285 rpm was reached. Duration of the fault was 2.1 seconds.

Calculations were made in an attempt to compare the event with values that engineering standards indicate a machine should be able to withstand for a negative sequence event. Engineers concluded that this event may have exceeded the requirements established by the standards but not necessarily at levels that would suggest severe damage occurred.

Limited visual inspection by experts revealed surface heating, as evidenced by burned paint, had occurred between adjacent slot wedges. Thus, some damage had occurred. Heat-affected metal was expected but couldn’t be assessed without disassembly. Investigators recognized that damage to the forging was possible, but viewed the tight-fit wedge design as having a positive impact.

The consensus conclusion was that the unit could be returned to service provided start/stop cycles were restricted until repairs could be made following a thorough inspection at the next outage in about a year. It appeared that the risk of continued service was not that a catastrophic failure might occur but rather that crack initiation and propagation might worsen the damage and increase the repair scope.

That’s about what happened. Disassembly about 14 months after the event revealed a greater number of burn marks than the optimistic best-case projections based on the partial inspection. Surface discoloration suggested worst-case heat-affected regions were concentrated at wedge-to-wedge interface areas rather than wedge-to-forging areas.

Topics addressed by other user presentations included the following:

DC resistance testing provides the capability to detect high-resistance joints, corroded conductors and connections, poor-quality connections, and shorted turns, a highly experienced engineer told the group. Instrumentation capable of very low resistance measurements with sufficient accuracy, precision, and resolution is required and the speaker provided desirable specifications. Next, the expert outlined a test procedure and reviewed three case studies. Access the presentation for details.

Endwinding looseness in small machines was the subject of another presentation available in the Power Users library. It covers inspection findings, planning, analysis, repair, and recommendations.

GVPI (global vacuum pressure impregnation) stator ground fault. Lesson learned concerned the need to inspect NGT cable for shielding and grounding.

Brushless exciter component failure. This is a “how it really happened” case study that begins with the generator protection relay tripping the unit on “loss of field.” The root cause of the problem was found to be a diode module that had failed in such a manner the generator field was shorted out of the circuit. The diode modules were rebuilt with new diodes and fuses.

Lesson learned by the presenter was that the sizing of fuses for this application was not so simple as one might expect. In this case, the extended exposure to heat created a condition in which the diode shorted but the fuse did not open.

In-service failure of an AeroPac II generator attributed to a breach of FME (foreign material exclusion) procedures. No obvious findings were in evidence from an initial visual inspection but electrical testing revealed a grounded phase. The field was removed and metal BBs and other debris was found at the bottom of the frame under the core of the generator in the 6 o’clock position. A section of the core had melted. A dead-blow hammer was discovered midway in the stator and determined to be the cause of the failure.

The second half of the presentation covered repair options and plan of action. The path taken: The extent of the failure and unknowns in restacking a GVPI unit prompted the owner to swap out the failed generator stator (and rotor) with a spare available in company storage. The equipment, manpower, and schedule required for this effort are detailed in the presentation. FME controls in place at the power producer’s plants were reviewed and modified to avoid a repeat.

Controls: PPCUG2020, Week One Recap

By Team-CCJ | February 21, 2022 | 0 Comments

The annual conference of the Power Plant Controls Users Group was conducted online for the first time this year. The two-week event, exclusive to owner/operators, began November 10 with a program focused on user experiences and vendor presentations. The latter were limited to 30 minutes each and conducted in two half-hour sessions. Each vendor was assigned a “breakout room” and users were connected to their presentations of choice. While attendees could not participate in more than two vendor presentations during the live Week One program, all presentations—both user and vendor—are available now on the Power Users website, mostly in video format.

Highlights of the Week One user and vendor presentations, developed by the editors, are below.

Week Two (November 17 only) was GE Week, characterized by meaningful technical presentations, Q&A, and open discussion on topics of interest to the user community. Those presentations can be accessed through the OEM’s MyDashboard website. PPCUG2020 concluded end-of-day November 17.

PPCUG2020, Week One user presentations

User presenters wasted no time getting granular in reporting on their plant and portfolio level experiences with GT exhaust thermocouples (t/cs), corporate digital transformation programs, control system and logic mods to support deeper cycling automation, Mark VI control system upgrade, and steam turbine/generator initiated generator purge.

Exhaust thermocouples in 7F machines have been a source of operating issues and instrument failures for years. One combined cycle reported on multi-unit experience with a spring-loaded t/c replacement design. No failures were experienced for the first five years. After that, the plant experienced rapid failures on one unit, then another. You’ll have to access the presentation on the Power Users website to get the details. The plant has not “given up on the design.”

Digital transformation. Big owner/operators often implement big portfolio-wide programs. A representative from one of America’s largest electric utilities reported on progress with its digital transformation program. Truly massive in scale, it includes in-house built sub-programs for digitizing work optimization, work orders, lockout/tagout (LOTO), drone management, machine learning for critical assets, and a reporting, documentation, and comments platform organized to specific plant components and subsystems.

To head off heat-recovery steam generator damage from cycling, one plant reported on modifying the control elements and logic of its originally designed baseload combined-cycle unit to achieve greater automation and avoid the inconsistencies of manual operator intervention. Three focus areas are condensate removal through HRSG drains, attemperator sprays, and damage monitoring. Much of the work in the attemperator area was based on recommendations from an EPRI report.

In upgrading from a Mark V to a Mark VI to solve obsolescence issues, this combined-cycle plant, equipped with four gas turbines, also installed GE’s digital platform. Goals were to use the same control system for all the turbines onsite; make the logic easier to read and consume; minimize HMI changes; share EGD (Ethernet global data) signals; monitor, track, and document relevant test data and results; and automate frequent testing procedures such as lift oil system and emergency bearing oil pumps.

The GT generator remote auto-purge system at this plant never worked properly, and staff wanted to make it operate the way it was supposed to. Fortunately, engineers found a few unused contact outputs in the H2 controls cabinet, upgraded the firmware, added sensors for other purge gases like CO2, and integrated the purge sequence into a graphical interface. Once this was done, operators wanted a similar capability for the steam turbine/generator purge. The remote feature is especially needed in this location because of the frequency of severe weather events—such as hurricanes.

Some of the hair-raising in-field piping configurations, different from design, and discovered only when hardware mods were made, can only be appreciated from the presentation, available to users on the Power Users website. You probably guessed that when operators at other plants learned about the new ST/G remote auto purge system, they wanted one too, so engineers designed one for non-GE units.

PPCUG2020, Week One vendor presentations

Vendor presentations focused on flexibility strategies, small and large control system solutions for gas turbines, integrated control and monitoring solutions for older facilities, legacy controls support, and single-point-of-failure analyses.

Siemens Energy’s Galen George addressed a round-robin of options for achieving flexibility when a combined-cycle plant’s load curve shifts because of renewable energy coming online in the market or service territory. Siemens’ Jim Badgerow supplemented the discussion by illustrating how battery energy storage systems can work with traditional GT plants.

PSM reviewed how the company’s Autotune rack-mounted controls solution, now 10 years mature in version 3, can satisfy small goals, like saving minutes on a simple-cycle unit startup, and large ones, like customizing a unit for greater fuel flexibility, capacity augmentation, and better turndown. Autotune is a machine-learning solution—it captures data from successful and unsuccessful starts/load change events. Need for tuning decreases as learning progresses.

MD&A’s Michael Broggi, along with Craig Corzine, CSE Engineering Inc (MD&A purchased the rights to CSE’s IBECs HMI platform), touted IBECs ability to integrate disparate control systems in older plants—such as turbine excitation, continuous emissions monitoring (CEMS), vibration monitoring, gas condition monitoring, generator relays, auxiliary PLCs, and balance of plant. Critical areas for success focused on by the presenters are time synchronization, sequence of events, high-speed data transmission versus historian-type data rates, data export, encryption, alarms, and reports.

TC&E’s John Downing presented his firm’s capabilities with digital front ends (DFE) for exciter controls. The company boasts over 200 Innovation Series load commutated inverters (LCIs) with DFEs. TC&E has partnered with Basler Electric and Emerson for full exciter replacements. Some of the additional reliability scope can include water-cooled busbar and resistor components testing and replacement; check valves, 3-way pump valves, and other pump panel components, and Nato board replacement.

Gas Turbine Controls. Capping Week 1, Chief Engineer Abel Rochwarger addressed solutions for GE TIL-1524 (when one exhaust TC fails high) and GE TIL-1275 (high P2 pressure control), as well as for speed-pickup spikes, date cards from 1990-2001, and other cards in the Mark V and VI control systems.

Cemtek KVB-Enertec’s Gary Caccciatore discussed the benefits of using the company’s cross stack TDL/DOAS technology to measure O2, CO, CH4, NOx, and NH3 on gas-turbine inlet monitoring in pace of the typical extractive CEMS technology. Advantages include immediate response time, accuracy, and reduced CEMS maintenance and spare parts.

Steam Turbines: STUG2020, Week One Recap

By Team-CCJ | February 21, 2022 | 0 Comments

The annual conference of the Steam Turbine Users Group is being conducted online for the first time this year. The four-week event, exclusive to owner/operators, began November 11 with a program focused on user experiences and vendor presentations. The latter were limited to 30 minutes each and conducted in two half-hour sessions. Each vendor was assigned a “breakout room” and users were connected to their presentations of choice. While attendees could not participate in more than two vendor presentations during the live Week One program, all presentations—both user and vendor—are available now on the Power Users website.

Highlights of the Week One user and vendor presentations, developed by the editors, are below.

Week Two was GE Week, characterized by meaningful technical presentations, Q&A, and open discussion on topics of interest to the user community. Those presentations can be accessed through the OEM’s MyDashboard website.

Week Three’s program begins on Wednesday, December, 2 at 9 a.m. Eastern with the first three hours allocated for private meetings with vendors; schedule these online just as you would a doctor’s appointment. Presentations by users are next, from noon to 2 p.m. followed by these two hour-long live vendor presentations with Q&A:

    • MD&A, 2 p.m., “Using Turbine Performance to Improve your Maintenance Strategy.”
    • Shell Lubricants, 3 p.m., “Choosing and Maintaining Lubricants for your Steam Turbines.”
    • A virtual vendor fair, complete with video chat rooms, runs from 4 p.m. until the end of the day’s program at 5.

STUG2020 concludes with the Week Four program on December 9. Program format is the same as that for December 2. The featured vendor presentations on the last day of the conference are these:

    • Arnold Group, 2 p.m., “Advanced Steam Turbine Warming for Increased Startup Flexibility.”
    • EthosEnergy Group, 3 p.m. “Multiple Upgrades Improve Reliability of a D11.”

STUG2020, Week One user presentations

“D11 Last-Stage-Bucket Inspections and Findings” at five plants suggests that leading- and trailing-edge erosion of L-0 blades is driven by operating hours and exhaust temperature versus starts. More specifically: The fewer the hours and the higher the temperature the less erosion. Inspections indicate that stellite shielding noticeably reduces the erosion rate, moisture-removal troughs in the last-stage diaphragm do as well.

Other findings are the following:

    • Erosion rate for combined-cycle turbines is higher than for steamers at coal-fired plants, in most cases. Plus, trailing-edge erosion is more prevalent in the combined-cycle fleet.
    • Erosion proceeds quickly after COD, then slows. Thus, if you blend out surface irregularities, the airfoils actually erode faster than they would have had you left them alone.
    • The highest level of erosion typically occurs from the top of the blade to 3 in. below it.
    • Blade damage is related to the moisture content of the steam more so than water chemistry.

Experience with 40-in. titanium L-0 blades—Case History One. Owner/operators of Toshiba steam turbine/generators received an alert in fall 2018 regarding the failure of 40-in. titanium L-0 blades at a Japanese powerplant. The OEM recommended inspections every 24k operating hours or 600 starts.

Personnel from a US combined-cycle plant with two steam turbine/generators affected by the notification shared with STUG2020 attendees their inspection and repair experiences from spring 2018 through spring 2020. The two steam turbines (called ST10 and ST20) typically were starting 125 to 225 times annually prior to the alert.

Readers are reminded that the PowerPoint for this presentation is posted on the Power Users website and accessible only to owner/operators. With two steamers and two OEMs involved (GE, the gas-turbine supplier, provided some ST outage support), a review of the author’s slides may facilitate your understanding of this ongoing project.

A spring 2018 L-0 inspection done before the alert was issued revealed no crack indications. However, some trailing-edge wear was in evidence near the dovetails, as was some so-called “wormholing.”

A follow-up inspection of ST10 was conducted the following spring when the unit was out of service to correct diaphragm dishing. Results were dramatically different than those recorded a year earlier. This time, every L-0 blade had cracks emanating from wormholes—from two to three indications per blade to between 20 and 30. Plus, one airfoil had a 0.75-in.-long through-crack.

The titanium blades on the generator end of the machine were removed and were replaced with a pressure plate because a replacement row of blades was not immediately available. The trailing edges of the L-0 blades at the opposite end of the cylinder were checked by fluorescent penetration inspection (FPI), blended, and reinstalled. The emergency pressure-plate repair was effective with no vibration or thrust issues after restart. However, the loss of output was significant at about 17 MW.

Another advisory was released by Toshiba in mid-June 2019. It reported that low-load operation of the turbine increased the rate of trailing-edge erosion because of flow reversal. It also indicated the lower portion of the trailing edge, extending from the platform to about one-quarter of the way up the blade, was most susceptible to damage. Cracks initiated by fretting of the midspan snubber sleeve were identified as well. The fix there would be upgraded material.

The pressure plate was removed from ST10 in fall 2019, replaced with non-OEM refurbished L-0 blades except for one new GE L-0 blade. The unit achieved full capacity on its return to service following a low-speed balance.

Both turbines passed their trailing-edge FPI inspections in spring 2020, leading personnel to assume it would be smooth sailing until the major. But that did not happen as stress corrosion cracking of dovetails was found in ST20. Temporary pressure plates replaced ST20’s L-0 rows and the unit was returned to service with a reduction in output of about 40 MW.

ST10 was restarted with new L-1 blades, upgraded materials, and new locking hardware.

Attend STUG2021 to get an update on this project and others as well.

Experience with 40-in. titanium L-0 blades—Case History Two. Another combined cycle equipped with a Toshiba steam turbine then shared its experience with 40-in. titanium last-stage blades in a double-flow low-pressure section. This plant, which began commercial operation in 2005, was designed as a 2 × 1 facility but constructed as a 1 × 1, reducing the output of the 330-MW steamer to about 100 MW.

The owner/operator making the presentation bought this combined cycle in 2016 with 20k to 25k service hours and lots of time on turning gear.  There was no record of the plant having had an inspection to that point. The new owner inspected the ST’s last-stage blades in-situ during a valve outage shortly after purchase.

A major inspection was conducted in fall 2017. Plan was to visually check the last-stage blades, but during the outage the OEM recommended adding an eddy-current inspection. This was the owner’s first and last experience (to date) with 40-in. titanium blades. It sold the facility in 2019.

Most blades had worse-than-expected erosion of their trailing edges. The distressed area extended from the platform upwards about 20 in. and from the tailing edge inwards about ¼ in. Some blades also had leading-edge erosion to the same degree. Plus, one airfoil was found with a 150-mil-deep indication about 4 in. up from the platform.

Plant personnel attributed the erosion to multiple years of low-load operation—that is, low steam flow. What happens, the speaker said, is that the root section of the L-0 blades acts like a pump, pulling droplets of moisture back into the trailing edges of the airfoils. This phenomenon is described in the article referenced previously.

New titanium blades, including supporting hardware, were ordered for both rows of last-stage blades. Today there’s a two-year delivery time for these parts.

The following points were mentioned during the presentation and follow-on discussion:

    • Data provided by pressure transducers installed in the condenser hotwell, said one user, shows promise in helping to determine the degree of wear suffered by last-stage blades.
    • The general feeling of the group was that the leading edges of L-0 blades should not be blended to address erosion. Thinking on whether to blend the trailing edges, or not, was split 50/50.
    • Stress corrosion cracking is a concern and water chemists should be involved in decisions concerning the low-pressure section.
    • Do crawl-throughs and borescope inspections of the LP section at every opportunity.
    • Decisions on the lowering of backpressure during winter should be made carefully. Low pressure can exacerbate moisture formation and erosion. As one user noted, it’s a tradeoff between maintenance and additional power.

The speaker ended his presentation by noting that his company sold the plant a year after the major so he did not know when the blades would be inspected again and if they would be replaced with the ones on order.

STUG2020, Week One vendor breakout presentations

ARNOLD Group

Advanced Single-Layer Turbine Warming System

Pierre Ansmann and Norm Gagnon covered the basics of steam-turbine warming for increased startup flexibility in their breakout presentation, which began by answering the question, “Why install a turbine warming system?” Highlights of their PowerPoint, available on the Power Users website, include the following:

    • Maintenance and operational benefits.
    • Differences in warming-system arrangements.
    • System durability and reliability.
    • Importance of proper insulation for a warming system.
    • Controls.
    • Cost and schedule of the initial installation.
    • Periodic maintenance plan.

In their review of alternative warming-system arrangements, the duo rejected those integrating heating circuits in insulation blankets, installing the heater on a thin mattress below the blanket, and using glass-fiber-insulated heating cable. The optimal system for the upper casing, they said, is a heater on a metal-mesh baffle; for the lower casing, permanent mounting of heating cable below the split line.

Ansmann and Gagnon explained that the ARNOLD system features interlocking high-performance blankets which conform perfectly to the turbine surface. High-quality materials and manufacturing, and long-term high-temperature resistance, allow the company to guarantee reuse of its insulation system for 15 outages without a decrease in efficiency.

More than five-dozen thermocouples, strategically located on the turbine, ensure proper heating. Each of the 18 or so heating zones has t/cs installed on the heating wires to double check if the zone is responding correctly and at the specified temperature. Below every heating zone, multiple t/cs are mounted on the casing to confirm even heating of the turbine.

The speakers said the ARNOLD warming system can maintain your turbine in a hot-start condition for at least four or five days after shutdown. No preheating of the turbine is required prior to a restart within this time period, reducing startup fuel consumption and auxiliary power.

C C Jensen, Oil Maintenance

Remote Monitoring of Lube Oil and Diesel Conditioning

Oil conditioners/kidney-loop filters are known for their ability to keep oil, and the machines relying on it, clean and healthy. In his presentation, Axel Wegner shows you how to keep lube and diesel oils in top condition; plus, how to receive alerts as soon as anything oil-related drifts out of spec—such as cooling-water temperature, excessive wear of machine parts, ISO particle count, etc.

Wegner’s message is clear: The optimal condition-monitoring and filtration system for any machine and oil type allows you to identify problems remotely and to take action before they get out of control. This presentation is one you might want to consider sharing with your plant’s O&M staff during a lunch-and-learn session.

Intek Inc

Essential Monitoring for Quickly Identifying and Repairing Air In-Leak Sources

Collin Eckel presented case studies highlighting a new process that combines repair of air in-leaks—identified through a condenser helium leak audit—and condenser vent-line air in-leakage measurements using the company’s Multi-Sensor Probe (MSP).

Recall that the presence of helium at the condenser exhausters indicates a leak. Intek’s MSP, installed in the vent line between the condenser and exhauster, measures and continuously calculates the condenser’s total air in-leakage rate.

Data from the MSP allows users to narrow the search areas for potential leaks, thereby increasing the success rate for finding and repairing them, and reducing the time for doing so. As air in-leaks are repaired, the MSP’s air in-leak value indicates the size of the leak eliminated by subtracting the new value from the total air in-leakage rate recorded before the repair was made.

Nord-Lock Group

Solutions for the D11 Closure System, Coupling Bolts, and Casing Tensioners

Adrian Price discussed the company’s Boltight D11 closure system and casing tensioners, focusing on how these products can cut maintenance costs by reducing the time required for (1) accurate, damage-free bolting, and (2) the tops-on/tops-off process—from as much as several days to several hours.

Co-presenter Steve Busalacchi walked attendees through the EzFit coupling-bolt solution and its benefits: reduced downtime, accurate radial force, safer installation, and the ability to achieve preload with hand tools. He profiled recent cases demonstrating the technology’s value in the field; plus, the preemptive steps plant personnel can take to minimize flange-bolt faults in future maintenance situations.

Users reviewing Busalacchi’s presentation will benefit from a better understanding of the principles of mechanical expansion bolts—what they are, how they work, and how they mitigate the problems associated with fitted bolts.

Parker Motion & Flow Control Products Inc

Legacy Denison EHC Hydraulic Pumps and Steam Turbine Applications/Support

Steve Westmoreland, a senior design engineer at MFCP, had good news for users trying to get by with their Denison EHC pumps, typically used to provide the hydraulic power for opening/closing valves on steam turbines. The workhorse Denison PV-09, which dates back 70 years, is no longer offered. The pump is obsolete and parts are not available from Parker, which bought Denison in 2004. Plus, it is becoming increasingly difficult to rework existing parts.

Westmoreland introduced attendees to the Parker PV+ variable-volume piston pump, available in horizontal and vertical arrangements, as a replacement for the PV-09. The following benefits of the PV+ over the PV-09 were highlighted:

    • The pump/motor interface is a simple bolt-together process; no laser alignment necessary.
    • Response time has been halved.
    • Higher efficiency (volumetric and mechanical).
    • A hydrostatic saddle bearing/swashplate replaces wear-prone rollers and bearings.
    • Improved suction characteristics—especially important to units operating at high altitude.
    • Separate cooling/filtered-oil loop to cool shaft bearings and seal, and the hydrostatic bearings.

Siemens Energy

Advanced Crack Detection in Free-Standing Steam Turbine Blades

The risk of steam-turbine blade flutter increases at low loads and vibration monitoring can detect this condition, thereby allowing owner/operators to take corrective action with the goal of maximizing fatigue life. Think of this presentation as a primer on how blade vibration monitoring is implemented. It also discusses a proven technique developed by Siemens to detect cracks in free-standing blades.

Lifecycle Maintenance Planning and Execution for Reliability and Cost Control

The second presentation made in the Siemens breakout explained the company’s bid strategy and outage planning. The key message here was to begin planning as early as possible and engage the OEM’s experts, and others, to assist in decision-making.

Film-forming substances (FFS): The next frontier in cycle chemistry

By Team-CCJ | February 21, 2022 | 0 Comments

If you’ve been in the power-generation business for a couple of decades—and made your bones at baseload, coal-fired, water-cooled plants, in particular—you may believe you know all there is to know about Rankine-cycle steam/water chemistry. Perhaps that’s true, for that type of facility.

But with coal-fired plants being shuttered in increasing numbers you may find yourself transitioning to a combined-cycle facility starting one or more times daily and equipped with air-cooled condensers and designed for zero liquid discharge. This is a new ballgame with respect to chemistry. You can almost forget what you know; in any event, positively embrace re-education.

Neutralizing amines and filming products are relatively new to many in the industry because their potential for reducing corrosion in heat-recovery steam generators (HRSGs), condensers, and steam turbines was not of great importance to personnel at traditional steam plants operating baseload with tight control of chemistry.

In these days of must-take renewables they warrant consideration. If you attended either of the first two meetings of the HRSG Forum with Bob Anderson you likely are aware of how amines and filming products have benefitted some users. EPRI’s Steve Shulder provided a backgrounder on how these products work at the first conference. It’s a good primer on the topic and will answer some of your basic questions.

Next, access online at no cost, the IAPWS (International Association for the Properties of Water and Steam) Technical Guidance Document (TGD) “Application of Film-Forming amines in Fossil, Combined Cycle, and Biomass Power Plants” (TGD 8-16). This is said to be the first public guidance document published for the industry on the subject. It was developed under the leadership of Dr Barry Dooley of Structural Integrity Associates Inc, who serves as the executive secretary of IAPWS.

Dooley’s presentation at the first HRSG Forum included information that he would share at the First International Conference on Film Forming Amines and Products in Lucerne, Switzerland, two months later. The well-respected chemist and metallurgist chaired both the Lucerne and second (Prague, Czech Republic, Mar 20-22, 2018) topical meetings. The 2019 meeting will be held in Athens, Greece, next March.

It’s probably fair to say that the chemistry of amines and filming products is somewhere in the middle stage of development: Some things are known, but there’s a lot more to learn despite the use of some products for three decades. In fact, even the generic name associated with these chemicals has changed recently. Dooley told the editors that feedback from the 2017 Lucerne meeting indicated much confusion regarding the various terms used for film-forming substances—for example, film-forming amines (FFA), film-forming amine products (FFAP), film-forming products (FFP), and others.

So IAPWS used its leadership position in the international scientific community to adopt the term “film-forming substances (FFS)” shortly before the Second International Conference on Film Forming Amines and Products and then changed the name of the meeting to the Second FFS International Conference. It attracted some 70 participants from 30 countries, illustrating the increasing interest worldwide in understanding and applying FFS.

Under the FFS umbrella are two subsets of the technology: amine-based substances (FFA and FFP), and non-amine-based FFPs.

The second international meeting provided a highly interactive forum for the presentation of new information and technology related to FFS, case studies of plant applications, and open discussion among users, equipment and chemical suppliers, university researchers, and industry consultants. The key messages from that conference:

    • If everything is working well at your plant then consider really hard whether using an FFS will make any improvements. If not, consider that the application could cause problems.
    • One clear case for application: If the shutdown frequency of the plant is going to increase, FFS can (perhaps) greatly improve offline protection.
    • If you are considering use of an FFS for any application, be sure to read Section 8, “Operational Guidance for the Continuous Addition of an FFS,” of the IAPWS technical guidance document referenced above. It will help you avoid mistakes and potential problems.
    • Before applying an FFS to your plant, be sure its chemistry is well understood. Do not hesitate to hire one or more experts for advice before making a decision. Perhaps the biggest challenge facing users in FFS selection is the proprietary nature of these formulations. Suppliers typically are unwilling to disclose “what’s inside.” Don’t inject anything into the steam/water circuit that you are not completely comfortable with.
    • Get a thorough work-up on system chemistry before adding an FFS, this to develop a baseline condition for comparison purposes later.

FFS 2018 allowed plant owner/operators to get answers to many of their questions relating to the use of FFS from the assembled community of international experts. A panel session focusing on key questions and uncertainties about FFS got “two thumbs up” from several attendees.

Other conference highlights included the following:

    • Updates were presented on recent experiences at fossil, nuclear, and industrial plants worldwide. The experience at nuclear plants has been with octadecylamine (ODA), whereas a wide range of FFS is being applied to fossil and industrial plants. The experience of FFP on condensate polishing and methods of determining FFA on surfaces were discussed.
    • Attendees shared ongoing research activities at different international organizations concerning decomposition products of FFA, distribution of FFA, measuring/quantifying the concentration of FFS in cycle water, adsorption kinetics of film formation, and the effects of FFS on flow-accelerated corrosion (FAC).
    • Extensive discussions reviewed the possible benefits of using FFS. They also identified many problems still occurring worldwide in plants using FFS without the detailed knowledge suggested by Section 8 of the IAPWS TGD. However, there wasn’t much open discussion on these problems. One of Dooley’s goals for the next meeting is to dig deeper into specific experience issues.
    • Two main conclusions from the conference: (1) Hydrophobicity does not always equate to protection, and (2) FFS cannot be quoted as “reducing” FAC simply by indicating a reduction in monitored iron levels. Regarding the second point, there should be before/after data for any application, with supporting photos if possible.
    • The need for adapting sampling and monitoring concepts to the specific FFS chemistry applied was recommended.
    • Gaps in knowledge and topics for further research were identified. For example, fundamental work remains to better understand the mechanisms at play with FFS. This includes film formation kinetics, equilibrium and stability, film structure (that is, thickness or number of layers), how absorption is affected by other amines, and the correspondence to the reduction in corrosion rate.
    • Work is required to understand the mechanism of the interaction between FFS and surface oxides. This was discussed as “interfacial science” and should involve the interaction of the FFS film with existing surface to include, initially, Fe3O4, Fe2O3, FeOOH, CuO, and CuO2. Also needed is work on the interactions that occur under feedwater conditions up to about 575F, where magnetite is soluble.

HRSG experience, issues typically global in nature

By Team-CCJ | February 21, 2022 | 0 Comments

So you switch hemispheres in both directions, west to east then north to south, and you discover that the pesky HRSG operational issues and concerns you are familiar with are much the same everywhere.

The 2018 Australasian Boiler and HRSG Users Group (ABHUG) Conference and Workshops, held last November, confirmed this view. The organization’s 11th annual conference in Brisbane, Queensland, chaired by Barry Dooley of Structural Integrity Associates Inc, provided an interactive forum for new information and technology specific to HRSG challenges in combined-cycle plants. There were in-depth case studies on plant issues and possible solutions, and pointed discussions among equipment users, suppliers, and international industry experts.

The more universal interactions focused on:

    • Cycle chemistry, instrumentation, and flow-accelerated corrosion.
    • HRSG thermal transients.
    • Oxide growth and exfoliation.
    • Attemperators, condensate return, superheater (SH)/reheater (RH) drain management.
    • Steam-turbine bypass operations.
    • Experience and research into the evolving field of film-forming substances.
    • Awareness and detection of air in-leakage.
    • Activities of the International Association for the Properties of Water and Steam—in particular the organization’s Technical Guidance Documents (TGD) of great value to powerplant owners and operators, which can be downloaded online at no cost.

Highlights of the meeting are summarized below.

Steam-drum cracking. Presentations included several case histories of HRSG steam-drum cracking, occurring primarily at drum-to-downcomer and circumferential welds. Inspection methods included visual, phased array, magnetic particle, ultrasonic, replication, and hardness.

Poor control of rolling and heat treatment of the original materials were highlighted as culprits, followed by weldability concerns. A summary point on weldability: Parent-material properties are dependent on manufacturing parameters for high-strength low-alloy (HSLA) steels, and welding introduces heat that disrupts the parent-material microstructures. Proper microstructures cannot be regenerated by post-weld heat treatment. Repairs, when required, can be problematic.

The common root cause was summarized as reheat cracking propagated by corrosion fatigue. The use of HSLA steels (for reduced wall thickness and increased allowable stress) contributes to this problem because of a unit’s higher operating stresses and material susceptibility to reheat cracking.

Fitness-for-service issues were reviewed that consider stresses caused by pressure, the simple weight of water and steam, and thermal effects of startup and shut down.

Reheater tube failures were examined for a 760-MW 2 × 1 combined cycle commissioned in 2002. The subject three-pressure, three-module HRSG does not have duct burners.

This presentation of a unique reheater-tube failure mechanism may be the precursor of many future mid-life failures in other HRSGs. The tube adjacent to the gap between modules, and entering the lower outlet header horizontally, had clearly overheated as shown by the large internal oxide growth and exfoliation data base (Figs 1 and 2).

Metallurgical reports showed multiple circumferential and transgranular cracks at the ID of the tube, beyond the heat-affected zone, progressing toward the outside.

Discussions and details led to observations of progressively more rapid localized oxide growth and exfoliation (OGE). Various hypotheses and further analysis steps were reviewed. The key takeaway was the following proposed sequence of events:

1. Normal steam-side oxide growth during years of operation.

2. As oxide thickens and insulates the tube internal surface from the steam, tube metal temperature increases, as does the oxide growth rate.

3. Tubes adjacent to the mid-module and sidewall gap operate hotter, and grow oxides faster than other tubes.

4. Eventually the oxide buildup reaches a critical thickness and it exfoliates.

5. In the case described, exfoliated oxide plugged, or partially plugged, the horizontal section of tube resulting in severe overheating.

6. Severe overheating and thermal-transient-driven strain at the failure site further accelerated localized OGE, thinning the tube wall and resulting in failure.

Learn more about this failure and OGE from Dooley at the upcoming HRSG Forum with Bob Anderson, July 22-25, 2019, in the Hilton Orlando.

Inspection after four years. A comprehensive presentation was given on pressure-vessel inspections at a combined-cycle plant after four years of operation, covering all major systems and their components.

The unit’s cycle chemistry includes all-ferrous feedwater metallurgy, AVT (O), solid alkalizing agent added to the HP and LP evaporators, no condensate polisher, and low iron level in the feedwater. Inspection methods, including commissioning and beyond, were described.

First in-service inspections (2015) showed loss of wall thickness in the HP economizer headers (one unit) and cracking in HP and LP drums (second unit), two-phase FAC in the condenser, and liquid impingement erosion of L-0 turbine blade row and shroud.

Water-chemistry management was reviewed, revealing a lack of trained personnel, lack of water-chemistry documentation, insufficient sampling and testing, and insufficient instrumentation to meet the recommendations of IAPWS published in its TGD 2-09. Improvements began, and by 2018, water-chemistry management was considered “close to normal.”

With chemistry management improved, the plant will concentrate on more active in-service inspections, and a proactive risk-based analysis approach.

HP drum replacement. The conference organizers called this “A great example of successful significant HRSG plant engineering projects—specifically, a total HP steam-drum replacement in a triple-pressure unit with key learnings outlined and shared.”

The HP drum at Tallawarra in Australia was replaced in 2018, after cracks were discovered in 2013 (just four years after commissioning). Deep cracks were discovered in various parts of the drum (risers and downcomers).

The cracks aligned with the fusion line between the weld and the drum and were determined to be blunt and oxide-filled, most likely the result of original welding defects—for example, a lack of sidewall fusion in the weldment to parent material.

The repair option was considered, but would mean a long outage (112 days). Even then, there was risk of not fully resolving the issues. This option was declined. Tallawarra was determined safe to operate (with adjustments) in the short term, and drum replacement planning began.

The challenges. An intensive two-year program was set that included factory visits and documentation reviews, stringent weld procedure and welder qualification checks, material certificates, reviews of heat treatment and hydrostatic test procedures, and clearly defined hold points.

Site preparation included risk-assessment workshops (including health and safety) and mitigation strategies based on workshop outcomes. Material handling challenges included a ground-to-height distance of 100 ft, anchor points with drone location reviews, and physical separation of multiple working levels (three above the drum floor, one below). Height restrictions from a nearby airport called for adjustments to the lift plan.

A key takeaway from this presentation was lessons learned. Engaging contractors in the work-assessment workshops was given high marks, as were real-time opportunities for safety strategies and improvements.

The drum was replaced within the scheduled period of 58 days.

An attendee with relevant experience told the editors afterwards that the drum-replacement plan presented certainly was one a similarly affected user might consider—provided his or her site could accommodate the cranes necessary to remove and replace the drum.

However, he said, he was not aware of a crack in a properly constructed drum-nozzle weld that has required replacement. While there are a lot of in-service cracks being found, the participant continued, he believes all have been successfully managed and/or repaired without removing/replacing the nozzle—thus far, anyway.

Editor’s note: ABHUG is supported by the International Association for the Properties of Water and Steam (IAPWS) and held in association with the European HRSG Forum, the HRSG Forum with Bob Anderson, and the journal PowerPlant Chemistry.

HRSGs: Tapping global know-how to expand local options

By Team-CCJ | February 21, 2022 | 0 Comments

A special report by Consulting Editor Steve Stultz based on information shared at the HRSG Forum with Bob Anderson

The 2018 HRSG Forum with Bob Anderson, held in Houston, March 5-7, like its predecessor in Charlotte, captured the topics of immediate interest to HRSG experts and combined-cycle system owner/operators. There were spirited discussions before, during, and after the formal technical agenda. Participants networked freely within this consolidation of equipment details, operating trials and errors, and forward-looking ideas. More than 40 exhibitors were present for specific discussions.

The report that follows is divided into these sections to facilitate access to information of greatest importance to you:

    • Inspections by drones, benefits of 3D printing.
    • Desuperheater issues? Longer attemperators might be a solution.
    • FAC remains the No. 1 problem for HRSGs.
    • Recent developments in film-forming substances.
    • Heads-up: Beware residual elements in advanced alloys.
    • HRSG lifetime assessments.
    • Monitor bypass-valve erosion to assure proper sealing.
    • The continuing evolution of controls and automation.
    • Protect against high SH/RH metal temperatures.
    • Miscellaneous topics: drum level control, tube-to-header weld evaluations, exhaust casings, steam-cooled attemperators, capacitance sensing.

Many of these topics are of worldwide interest and are being discussed at the Australasian HRSG Users Group (AHUG), the European HRSG Forum, the Canadian HRSG Forum, and other such regional meetings. Information transfer to the US meeting is by way of Bob Anderson and Dr Barry Dooley of Structural Integrity Associates Inc, who actively participate in those conferences as well.

To illustrate, a full-day workshop at the 2017 AHUG meeting was dedicated to materials issues in HRSGs, the same concerns addressed in Houston. Topics included P91 damage mechanisms and case studies (CSEF steels), failure mechanisms, life-prediction and remaining-life assessment methods, weld repairs, and oxide growth and exfoliation of HRSG materials. Open discussions at the 2018 HRSG Forum, led by Anderson and other members of the steering committee, focused on these issues as well.

The third annual HRSG Forum with Bob Anderson will be held at the Hilton Orlando, July 22-24, 2019, where you’ll learn from the world’s leading experts on HRSG design, operation, maintenance, inspection, water treatment, layup, etc. Program development is in the formative stage. Visit the organization’s website in the early fall for important details.

Inspections by drones, benefits of 3D printing

Innovation spawns innovation. One technology advancement presented at last year’s inaugural HRSG Forum with Bob Anderson was inspection by unmanned aerial systems (UAS), a/k/a drones. Xcel Energy’s Scott Wambeke explained how these inspection tools were flying within the congested spaces of HRSGs, launching new dimensions in this cost-effective and time-saving technology.

Pilot skills had been established outdoors along vast transmission lines, then within the relatively open spaces of large coal-fired utility boilers, verifying the values of these recorded flights. Now, spaces were tight but beneficial results were expanding.

Returning this year, Wambeke explained the escalating benefits of 3D printing, an innovation developed while bringing UAS skills and benefits to Xcel’s full power-generation fleet. So what began as plastic drone parts has expanded into project planning and execution.

Working with a local university, Wambeke’s team has mastered specific drone-system improvements, driven in part by equipment damage during the all-too-familiar impact events. One fast-growing need has been replacement and more durable blade guards. Another has been customized attachment systems for prototype lighting.

The licensed outside flight crews at Xcel use some elaborate systems and equipment, and travel long distances in their investigations and inspections of power lines, rights of way, and similar tasks. The inside teams at Xcel began with less expensive, off-the-shelf commercial drones, often making their own repairs. “Every time we fly in these tight areas,” explains Wambeke, “we know that there’s a 30% chance of drone damage.” Their drones are still considered consumable inspection tools.

Then the team purchased its first 3D printer. Repairs were made more quickly and innovation opportunities began. “One critical advantage is being able to make improvements as you go,” said Wambeke. “You can print a component, try it, improve it, and quickly try it again.”

Last year’s presentation concluded with a forward look at drone system advancements, and expanded applications. Both developments are moving quickly.

Navigating to projects: An operating HRSG was experiencing repeated failures in preheater 1, row 2. Access clearance to the failures at the lower header was tight at 1.6 in. The boiler/HRSG group was investigating a new printer and decided to try 3D printing. Engineers would look at 1:20-scale components.

When printing was done, project planners were able to see (and show to management) the processes for cutting header piping and drains free, then gaining access for repairs. The models also would serve as planning tools for NDE and provide tube-to-header joint geometry familiarization to the welding crews. In sum, the simple 3D printing process became proof of concept for what was deemed a five-day outage.

Said Wambeke, “This became an excellent tool for both planning and the actual repair. The project was finished ahead of schedule in four days.”

Wambeke concluded with a review of 3D printing hardware, use of dissolving media, and the joining of parts by friction welding. He also noted that 3D scanners can replicate geometries to help reverse-engineer old parts when drawings are not available.

Questions and discussions were varied. Small blimps also have been considered for inspection flights, but achieving lift is difficult without supplemental fans, and internal drafts can make stability difficult. Work on drones and options continues. One additional note: Printer plastic is priced well below printer ink.

Longer attemperators speed up spray evaporation to mitigate pipe cracking

Paul Lofton, Tampa Electric, and Ory Selzer, IMI-CCI, discussed HRSG attemperator replacements at two TECO Bayside power blocks installed during the “bubble” (2003 and 2004).

This presentation discussed systems for:

    • HP (main steam) to cold reheat (CRH) bypass.
    • HP (main steam) interstage.
    • IP (reheat steam) interstage.

During a walkdown, a crack was discovered in the circumferential weld at the HP-to-CRH pressure control valve. This indication was discovered completely by accident while escorting a vendor across the top of the plant. The weld was cut out and replaced.

An HP interstage attemperator then showed girth-weld indications during linear phased-array UT inspection of the P22 pipe. One indication, 8 ft down from the spray nozzle, was 0.625 in. deep, originating from the inside wall and progressing toward the outside, approximately one third of the way around the pipe. All systems on both units were then inspected.

Plant layout fortunately allowed room for longer attemperator steam pipes. Seven new attemperators were purchased, twice the length of the old ones for improved dwell time to evaporate spray-water droplets. The resulting 16 to 18 ft total length gives more time to prevent quench damage. Four radial spray nozzles replaced the single nozzle of the original design; the existing 180-deg elbows were reused.

All modifications were designed to provide added strength and life in cycling duty. The common theme: conventional equipment is rarely designed for cycling. System improvements included longer pipe legs, improved drain systems, radial nozzles, Stellite 6 hard-faced seats, and new actuators.

Many questions followed regarding thermocouple locations relative to welds. There were also extended questions and discussions about cycling impact on original designs, steam versus water atomization, modification costs and methods, OEM design variations, and overall design and repair options. Dig deeper with a recent CCGT case study: Pipe Repair Oddyssey. 

FAC remains the No. 1 problem for HRSGs

Structural Integrity’s Dooley provided an in-depth presentation on “the No. 1 problem” for HRSGs: flow-accelerated corrosion (FAC).  He reiterated the chemistry influences on FAC, typical locations, appearances, and common mistakes in attempts to identify and control. “The problem is global, and it’s not just the power industry,” Dooley stressed.

Background discussion included temperature ranges and the solubility of magnetite, timing of first appearance in both vertical and horizontal gas path units, and turbulent flows at bends and complex geometries. Air-cooled condensers also were addressed.

“It is very important to identify what type of FAC you have, because the two types (single- and two-phase) are controlled by different aspects of the cycle chemistry,” he stressed. Many examples of appearance, location, and damage level were shown and characterized in detail.

Treatment options (and overall system chemistries) were discussed along with relevant IAPWS guidance documents. Component materials were also discussed, as were film-forming substances (FFS) that might help in protection. These would follow in a later presentation.

Recent developments in film-forming substances

EPRI’s Stephen Shulder addressed the increasingly dynamic topic of FFS for corrosion resistance and layup protection.  This topic now has its own international conference, most recently in Prague, organized by IAPWS.

Shulder offered background. Amine/filming chemistry is being used or considered for many reasons, including:

    • Better layup protection during outages of varying duration. Film-forming substances can place a hydrophobic barrier between metal surfaces and liquid. Limits on capital expenditures or personnel could restrict the full use of dehumidified air systems, a viable alternative.
    • Non-optimized corrosion-product transport with recommended feedwater treatment programs. Cycling operation means more startups, and excessive use of ammonia can lead to vapors within the plant and short polisher runs.
    • Two-phase FAC damage. Neutralizing amines may provide better dissociation and distribution than ammonia, and higher localized at-temperature pH.

The EPRI chemist discussed filming amines and filming products, amine chemical structure, and application benefits and risks. He then turned to case studies, including potential impact on and benefits to air-cooled condensers.

Considerable time was spent on the details of FFS research, followed by storage, feed considerations, and application schedules. His key two-part message:

1. Any use of film-forming substances should be in combination with, not in lieu of, best cycle chemistry by international standards.

2. You can’t control what you can’t identify and measure.

Shulder ended with a list of questions to ask any FFS supplier.

Dooley added that “There is a whole series of failures that can occur with these substances,” and reiterated that a definitive consensus document is now available at no charge through IAPWS, namely Technical Guidance Document “Application of Film-Forming Amines in Fossil, Combined Cycle, and Biomass Power Plants” (TGD 8-16).

Beware residual elements in advanced alloys

One shot across the bow at last year’s inaugural HRSG Forum was a report by Jeff Henry, Applus+ RTD.  The topic: advanced alloys. The message: We now have residual elements in the steel to consider, and they’re changing the material chemistry on a microscopic level.

Returning in 2018, Henry offered an update on the evolving issues with creep-strength-enhanced ferritic (CSEF) steels. His theme remained the continuously changing knowledge base, and the need for related ASME Code updates.

One initial Code focus is a reduction by ASME in the allowable stress for P91. According to Henry, who chairs the ASME Section II Committee, “reductions are now approved by ASME and will be in the 2019 edition of the Boiler and Pressure Vessel Code. Modified chemistry for Grade 91 Type II, currently a code case, could be released at the same time.”

However, he explained, the Code does not adequately address heat-treatment specifics for these steels, even after 20 years of experience and data. “Heat treatment remains an important topic, and many questions are the same now as they were 20 years ago.”

As he explained in 2017, CSEF steels are relatively complex materials and can vary according to their production process, “depending on heat-specific chemical composition and processing histories.” This is where the interesting and disturbing topic of recycled materials appeared last year.

For clarity, Henry stated: “The degree of technical control required during all phases of implementation (design, production, manufacturing, and erection) is substantially greater than it is with traditional (that is, more tolerant) powerplant alloys, such as Grades 11 and 22.”

“Improper heat treatment,” Henry stated, “has been the single greatest cause of unnecessary failures, repairs, and replacements” involving these steels—particularly Grade 91.

Such improper practices have cost the industry hundreds of millions of dollars, and will continue to do so as “poorly heat-treated components that have not been properly inspected continue to fail prematurely.”

This is not because of overly complex procedures or processes. “The requirements are not abnormally difficult to understand or implement,” Henry explained. “Rather, there has been too little effort made to understand how the basic metallurgy (microstructure) of this class of steels dictates successful heat-treatment practice.”

The industry is now left with many questions, including these:

    • How many times can these materials be heat treated?
    • Can poorly heat-treated materials be salvaged?

Henry followed this with a detailed review of typical heat-treatment processes, and various complicating issues. As one example, the Code specifies minimum hold times for post-weld heat treatment, but not does not specify maximums. For temperature, he explained, the Code sets an upper limit, above which a material should be rejected. But the intention was never to hold material at this temperature. “Code needs to review this,” he stated.

Many questions and discussions followed (as they did last year) including precise temperatures, cooling durations, weld inspections, impacts of wall thickness, adjacent materials, weld materials, and the benefits and risks of re-austenitizing.

“Austenitizing can reset the life clock,” explained Henry, “but may not duplicate original material properties.” EPRI’s John Siefert took this further. “If creep damage is present, you cannot restore the material to virgin conditions.”

Henry ended with a case history of salvaging improperly heat-treated Grade 91 large-diameter (28 in.) elbows.

More questions followed on weld repairs, inspections and acceptances, and the global state of (or lack of) knowledge. The questions and discussions made clear the obvious concerns about these material properties, their complexities, and their quality issues.

And a key question: How do we track all of the actions that have taken place on all the pieces and parts that we have? The awakening answer: Even looking back at the original materials, there is a lot that we just don’t know. The best advice is to keep good records of everything you can.

HRSG lifetime assessments

“HRSGs are millennials,” suggested Sargent & Lundy’s Danial Azukas, meaning that most of those operating today were built in the 1990s and early 2000s. They were base-load designs for 30-year operation (300 cold, 1500 warm starts, and 6000 hot starts).

Then gas prices fluctuated, both up and down, and green power entered. As discussed throughout the HRSG Forum, cycling and unanticipated owner/operator challenges began.

Azukas discussed various cycling impacts through a case history, launching a theme of cycling and remaining life assessments that would appear throughout the organized meeting and the frequent open discussions.

One assessment element discussed was benchmarking with data and evaluations not tied directly to the subject plant. The North American Electric Reliability Corp maintains availability database systems that can add value to such reviews, highlighting outage events and other influencing data. Peer plant comparisons of outage factors, availability and capacity can also help in the look forward.

Assessments would become a common topic throughout the conference.

Tom Sambor, EPRI’s technical leader for Program 88 HRSG and BOP, discussed life assessment of boilers and pressure parts, particularly the fleet of HRSGs now reaching the soft design life.

Reviewing relevant background, he explained that in Western Europe fitness for service was “an integrated approach to operation and life management.” Re-assessment for continued operation was common, he explained, due in part to long-term use of more complex materials.

This is not the history in the US and Canada. He explained that in the 1980s and 1990s, service fitness became an urgent need in North America because of header ligament cracking, dissimilar metal weld failures, and some catastrophic material events.

EPRI began pioneering with its RP2253 project.

Sambor explained that EPRI now advocates a seven-point life management approach:

1. Understand how design, operation, fabrication, and metallurgy affect component performance.

2. Appreciate the historical issues (failures, statistical analysis).

3. Develop optimum specifications.

4. Set improved quality guidelines for design, manufacture, and operation.

5. Determine when, where, and how to look for damage.

6. Develop component-specific methods for repair/replacement that exceed minimum ASME Code rules.

7. Employ technology transfer of information to codes, standards, and the global community.

His presentation concentrated on the search for damage.

Another bit of history: The Central Electricity Generating Board (CEBG) in the UK performed foundational work in power-generation fitness for service in the 1960s. “Thousands of welds were identified to have fabrication flaws,” explained Sambor. “Rather than simply repair or replace, the CEGB chose to evaluate.”  Assessments looked at “safe” versus “potentially unsafe.”

In the US, the wake-up catastrophic failure was in 1986, at the coal-fired DTE Monroe. The failure occurred in Unit 1. But Units 2 and 3 were not shut down. Both were needed to meet demand, and continued in reduced operation. This ongoing generation during assessment proved successful.

Sambor’s discussion centered on safe operation based on inspection results, and subsequent inspection planning. “In some cases,” according to National Boiler Inspection Code (Part 2), “a visual inspection of the pressure-retaining item will suffice. However, more comprehensive condition-assessment methods may be needed—including an engineering evaluation performed by a competent technical source.”

Detailed examples also are given in American Petroleum Institute’s API 579, Section 1.1.2. As Sambor explained, “By its own definition API 579 does not independently determine if a component is fit for service; it helps determine.” API 579 was released in 2000 and immediately received widespread acceptance both inside and outside of the refining industry.

Sambor explained further background and continuing activities, highlighting those by API and developments at ASME, specifically the Boiler and Pressure Vessel Code Main Committee. ASME and API now work together on the issues.

Then he presented specific examples of poorly performed fitness programs. Several cautions were discussed, including lack of communication and inherent limitations of some overly specialized consultants.

Sambor next focused on fitness-for-service challenges specific to HRSGs, including the following:

    • For operations: Cycling, and significant duct firing.
    • For materials: Extensive use of CSEF steels.
    • For maintenance: Plants are forced to “do more with less.”
    • Other: Gas-turbine upgrades can have unintended consequences on HRSGs (and other downstream equipment).

Sambor then discussed these specific component challenges:

1. Large branch connections. This has become a significant industry problem, particularly with Grade 91.

2. Tube-to-header connections. This has led to numerous drain evaluations for condensate removal.

3. Circumferential cracking at drum-nozzle toe welds is increasingly common.

Many related issues were discussed throughout the 2018 Forum, including valve bodies and attemperator-induced quench cracking.

Sambor ended with EPRI’s overall fitness philosophy, stating that proper methodologies must be:

    • Based on engineering rigor.
    • Relevant and no more complicated than necessary.
    • Benchmarked against well-pedigreed test cases from the industry.
    • Clear for key scenarios such as identified flaw, assumed flaw, creep (time-dependent), etc.
    • Based on well-maintained and relevant databases, and active sharing of both present and past information.

“Most of all,” he said, “safety must be paramount! Safety drives fitness for service.”

Lengthy discussions followed including hands-on training of inspectors (AIs) and increased interaction with insurance carriers.

Later in the program, EPRI’s John Siefert discussed technology-transfer achievements (and open information exchange) as an approach to equipment life management, specifically regarding CSEF steels. Looking back to 2006, he stated that “after 10 years of research and more than $15 million invested by collaborative industry projects, there is now sufficient insight to provide an integrated strategy for life management of CSEF steels. This includes more than 125 individual reports and the world’s most comprehensive understanding of these materials in powerplant components.”

He then repeated that “variability is a reality in 9Cr martensitic CSEF steels.” The inconsistency is in deformation and damage resistance. “This reality,” he stated, “increases the complexity of an integrated life-management strategy.”

Siefert outlined the resistance specifics and discussed the need for more stringent control of both up-front (heat-to-heat) composition and various material heat-treatment practices.

“One current emphasis,” he said, “is to merge two items of EPRI’s seven-point life management approach:

    • Understand how design, operation, fabrication and metallurgy affect performance, and
    • Transfer this information to industry codes and standards, and the global electricity-supply community.”

The presentation offered details on programs by EPRI, ASME, and NBIC, and included a list of publicly-available EPRI reports.

Questions included applicable codes for repair of older materials.

Monitor bypass-valve erosion to assure proper sealing

Bob Anderson discussed HP-bypass pressure control valves, stating that although these are considered severe duty, they can last 10 to 12 years before seat/plug repair, if properly controlled and operated. The primary concern is erosion caused by water and/or steam passing through the valve (HP to CRH). This is not a problem with all units, nor is it a problem specific to any valve OEM.

He began with a single-shaft unit example in somewhat unique operating modes including open cycle, then followed with a 2 × 1 plant in typical operating modes.

In the first example, the HP-bypass pressure control valve began leaking through after one or two runs.  Although correctly installed, the OEM modified the valve to improve erosion resistance, but rapid erosion continued. The issue was identified as part of open-cycle service when the gas turbine is at low load and the steam turbine is offline. This allows condensate to pool along the bottom of the main-steam pipe, shrinking it relative to the top of the pipe. The normal 1% slope downward becomes reverse slope.

In a second case study (2 × 1 in typical modes), leaking occurred after a period of years, and although modified by the OEM, recurred. Arrangement and start modes were reviewed. During a lag cold start, the bypass valve opens too early when main-steam temperature is still at saturation (Tsat). Delay in opening the PCV until 35-deg-F superheat is achieved should eliminate erosion damage. A bigger warming drain may be required (before the header isolation valve) to avoid excessive startup time.

The continuing evolution of controls and automation

Emerson’s Jim Nyenhuis provided an update on automation and controls for combined cycles. He posed this question: “How can automation help, based on the changing world of plant operations?”

The presentation began with a look at classic closed-loop controls, and an interesting point: Controls look in real time. So the key is to also understand system dynamics, including the elements of time. In one example, Nyenhuis looked at unstable final steam temperatures caused by cycling, and PID-based load control. The question: What can refined control do for the long-term life of the components?

“If we can develop very refined models,” he said, “this allows us to look forward and make predictions, then anticipate these in our controls strategy.” The in-depth presentation appealed to those knowledgeable in the systems and tuning processes, but also reinforced the movement toward more forward-looking operations (the cycling world).

Discussions highlighted the complexities, including these:

    • Predictive modeling should account for historical empirical data, weather, time of day, differing humidity.
    • Other units on and running.
    • Anticipating where the load will be in 20 to 30 minutes.
    • Other operational challenges, including justifying the cost of a control-system change to management.

Protect against high SH/RH metal temperatures

HRST Inc’s Bryan Craig explained the primary factors affecting HRSG superheater and reheater tube metal temperatures, and typical areas of concern.

“For some HRSGs,” he explained, “the highest tube-metal temperatures could be in Module 1, during low-load unfired operation. In HRSGs with duct burners,” he continued, “maximums will be in Module 2 with burners firing.” And why is this important? “A temperature increase of 15 to 20 deg F can reduce equipment life by half,” he stated.

Long flames and gas-temperature variations downstream of burners were discussed, and rule-of-thumb observations were given including duct-burner cameras.

Failing or missing gas baffles are also a major contributor, allowing high temperature exhaust gas to come in contact with downstream tubes designed for lower temperatures. Craig presented photos of numerous gas-baffle failures.

Gas-turbine upgrades can also push HRSG tube-metal temperatures above their design limit. Gas temperatures increase, but steam temperatures can remain constant, controlled by the attemperators.

Internal oxide growth also was discussed. During comments, Dooley mentioned that a workshop on materials and overheating was held at the Australasian HRSG Users Group, and was on the agenda for the European HRSG Forum, held recently in Spain. “We are discussing overheating in HRSGs as a serious problem, and looking at doing some proactive work, particularly with a large global database on oxides in various materials.” This will become a topic for the HRSG Forum.

Miscellaneous topics

Drum level instrumentation. Jim Kolbus, Clark-Reliance Corp, discussed recent developments in drum level instrumentation, and a focus on ASME Code requirements.

“The only direct-reading device is a gage glass,” he explained. “Indirect reading is a remote device.” He then reviewed the options, pressure limits of each, and Code-permitted variations.

The discussion included minimum Section 1 water-gage requirement—including placement details, isolation and drain valves, permitted globe-type valves, and chain operation mechanisms for personnel and plant safety.

Common Code violations and concerns discussed included:

    • Isolated inoperable water gages.
    • Missing water gage glass.
    • Missing illumination from water gages.
    • Inadequate display of remote indicators in the control room.

Kolbus stressed “proper maintenance and routine inspection of these critical instruments,” such as blowdown of small-diameter sensing lines to remove sediment.

Tube-to-header weld evaluations.  Matt Dowling of Applied Technical Services followed with a case study on HP/RH-tube-stub-to-header welds at the Ontelaunee Energy Facility. The F-class 2 × 1 combined cycle has accumulated more than 80,000 operating hours since COD in 2002.

History includes 73 failures, all in the upper-header bent tube rows. Analysis showed that damage initiated at the outer edge of the heat-affected zone, approximately 0/125 in. from the toe of the weld on the tube side.

Dowling covered the details of OD, ID, and mid-wall inspections, some difficult because of geometry. To date, 27 repairs have been completed, and further testing continues. Root cause is not yet identified.

Forum participants offered ideas and suggestions, and interesting insights going forward. This is a bubble unit; subsequent designs were modified.

Exhaust casings. Jake Waterhouse, Dekomte, presented exhaust-casing insulation inspection and repair examples for liner upgrades, insulation repacking, hot-spot elimination, apertures, and openings.

He began with cold-casing duct insulation issues (insulation loss leading to hot spots). Operational impacts highlighted the multiple negative effects of two-shifting and cycling including temperature transient fatigue and stress, movement, and dew-point condensation (acid and water).

Both standard and high-turbulence liner arrangements were described including the potential benefits of scallops. Duct insulation options included traditional, staggered, and stacked.

Pumpable repairs were described, including techniques and thermographic modeling during application. High-turbulence exhaust-diffuser repairs followed, including an example repair during operation. Fabric expansion-joint technology was described in detail for penetration seals.

Effective monitoring during plant operation was emphasized throughout the presentation and discussions.

Steam-cooled desuperheaters. Attemperators that cool with saturated steam were described, primarily interstage and final desuperheaters designed to reduce thermal shock damage. The design discussed by Karel van Wijk, Advanced Valve Solutions, has been in operation for 10 years.

Thermal-shock calculations reviewed estimate that by reducing temperature differential by about 125 deg F, the number of expected startups without damage increases enormously. Sample calculations and predictions were reviewed.

Desuperheater positions, designs, and materials were examined in detail.

Capacitance sensing. Qussai Metashdeh, Tech4Imaging LLC, discussed non-invasive imaging and monitoring technologies. He concentrated on electric-capacitance volume tomography (ECVT), specifically for two-phase flow applications in HRSGs.

Also discussed was adaptability to various locations, concentrating on evaporator steam quality for ramping purposes.

ECVT is also applicable for three-phase flow (water, air, oil) and work is being supported by the DOE’s National Energy Technical Laboratory.

Questions included solids monitoring (fluidized beds) and testing with hydrocarbons.

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