Attention to detail early in the HRSG lifecycle sets the tone for long-term reliable service

The first five years of HRSG operation are critical for building the foundation necessary to assure a reliable and satisfactory service life, said engineers from HRST Inc participating in an editorial roundtable with CCJ staff.

In the early years, they continued, control and organization of supplier documentation will benefit current and future decision-making. Plus, timely inspections and analysis can help ward off potentially damaging conditions or identify items to allow contract closure with suppliers.

As time goes on, analysis also can determine the effects of any current or impending changes to operations that were not planned when original specifications were prepared. Finally, there are commissioning and early operating practices and conditions that can harm the HRSG. Many examples are in evidence industry-wide, the experts said. Several are identified below.

First year

Focus plant personnel in Year One on gathering, organizing, and protecting documentation. Proper and efficient management of maintenance and operation require comprehensive and complete documentation, Team HRST said.

It’s important to confirm that all suppliers have submitted complete design packages. Developing a reconciled list of documents with the latest revisions and dates will prove invaluable as time goes on and personnel change. Obtaining copies of the ASME Manufacturer’s Data Report forms can verify component design pressures and materials of construction, and aid in future repairs.

ASME B31.1 requires every facility to have an inspection program for covered piping systems (CPS). This primarily constitutes pipe 4 in. diam and larger between the HRSG and steam turbine or user. The program calls for a comprehensive list of documents. B31.1, Article 141, “Operation and Maintenance,” provides guidance.

Confirm that the documents are complete, current, and well protected. Guard against catastrophic loss and assure ready availability by keeping complete sets of documents in multiple accessible locations.

Inspection, testing, analysis. Your pre-first-fire inspection should focus on design details, use of correct materials, and proper installation, and be supported with ample photography.

Inspectors should go through the gas-side access and crawl spaces, paying close attention to the inlet duct and firing duct. Violent exhaust flow is known to take down components in the inlet duct if they are not installed properly. Note interferences from restrained thermal expansion of tube bundles and duct liner systems.

Inspect each drum, paying close attention to the final (secondary) steam separator that covers the steam outlet to the superheater. The HRST engineers said it limits carryover of water droplets and impurities that can quench or plate out on downstream tube surfaces. Excessive carryover can lead to loss of superheat and elevated risk of tube damage from high temperatures. In severe cases, carryover may quench the tubes, causing fatigue damage at the header joints.

All pipe and pipe supports external to the HRSG must be in the correct position and any hydro-stops removed before fired operation. This is a good time to document the hot and cold marks, before they fade or fall off. If low points in steam pipe cannot be drained, consult the OEM or contractor.

First two years

Near the end of Year One, or just before expiration of warranty periods, a comprehensive inspection and test program is highly recommended by the HRST experts. It will provide baselines for future inspections. Photographic documentation is especially valuable.

Within the gas path, inspectors should look for signs of restrained expansion, interferences, and wear. Some cracks and twists can be expected and are often self-limiting. Others are signs of imminent or future trouble. Improper material selection or the occasional installation of the wrong material will often be revealed as a difference in oxide color or scale formation. If damage is found, this is the time to address the mechanisms conducive to future component failures.

Examples of inspection findings by Team HRST include the following:

Stressed tubes. Warped tubes are not necessarily a liability, but they are signs that the tube has been stressed and has yielded. Additional fatigue may cause failure. Cracking might be apparent in tube joints. Stress is common in the superheaters, reheaters, and economizers. Failures have been known to occur shortly after commissioning.

External tube wear. Tubes are susceptible to oscillation from forced vibration attributed to exhaust flow. A tube-tie support lattice typically is installed at multiple points along the height of the tube bank to limit this oscillation. If the tube ties are spaced too far apart or if they are loose, tube vibration causes fin wear, and eventually wear on the tube wall.

Overheated materials are those that have been subjected to a sufficiently high temperature for a length of time to cause changes in microstructure, or excessive scale formation. Perhaps the materials are mismatched to their location in the HRSG. Overheating typically is confined to the inlet duct and firing duct. Inspectors may find one liner sheet, gas baffle, or tube that looks out of place. If not corrected, early failures can be expected.

Duct burners. Look for signs of flame impingement on the walls or downstream tubes. Long flames or excessive localized heat can be caused by failed burner nozzles, inadequate fuel distribution, inadequate exhaust distribution, or improper controls.

Online inspections. There are several ways to identify areas of concern with the HRSG in operation, including these:

Infrared imaging inspections of the ducts—in particular the roof, doors, and pipe seals of the first three modules (HP evaporator and forward to the gas turbine)—can point to excessive casing temperatures where issues are likely to exist.

Monitor operation of the steam separators to verify their proper operation. Do this by testing for the purity of steam leaving the drums to ensure downstream equipment is protected against carryover.

Examine flames through the burner viewports to verify flame lengths are not excessive.

Review data in the plant historian to identify excessive cycling of valves, valve leakage, excessive desuperheater spray water, and other harmful conditions.

Walk-down high-energy piping systems to locate unwanted movement/displacement.

Second through fifth years

Every year or two after COD (commercial operating date), HRST engineers recommend a standard 10- to 20-hr inspection to look for wear issues throughout the HRSG. As conditions develop, they can be identified and the underlying cause corrected before large-expense outlays are required. After four years’ time, issues that tend to be time-dependent should get more focused attention—including corrosion, expansion-joint failures, pipe seal failures, and fatigue cracking of pressure parts and liner systems.

Analysis for vulnerabilities and changes. Flow-accelerated corrosion (FAC) may be the most detrimental and expensive of tube and pipe failures encountered by HRSG owner/operators. It is highly dependent on water chemistry. Damage from FAC can develop rapidly, with visual wear occurring in less than one year.

HRST engineers told the editors that the HRSG should be evaluated for FAC risk before the third year of operation. A follow-on FAC inspection plan can then begin. However, your mitigation program should begin earlier if there are telltale signs on FAC in the LP or IP drum in Year One.

While HRSGs are now constructed using FAC-resistant materials in high-risk areas; in those cases, the scope or frequency of inspection can be reduced—perhaps—but never neglected.

Operational changes. Several years after COD, the owner may need an operating profile different from that specified for the original design. This could involve a change in cycling frequency, operation at a lower load, etc. A thorough engineering evaluation of the new operating parameters on the HRSG is highly recommended by HRST engineers. Here are some things to think about as you go through this process:

Cycling study. Many specs require that the HRSG be designed for a certain number of starts per year. Each start contributes to wear and tear. A cycling study will look at those components vulnerable to thermal transients, high temperatures, and low flow rates that often accompany startup and shutdown conditions.

Bear in mind that cycles affect the allowable HP steam-drum ramp rate, so if startup time must be reduced or is in question, the cycling study will reveal the balance between cycle frequency and ramp rate.

Low-load operation. Operation of the gas turbine at low loads affects steam and water flowrates. This can lead to unstable flows in economizers and poor flow distribution in superheaters and reheaters, all affecting tube reliability. High exhaust temperatures from some turbines require excessive desuperheater spray that damages downstream pipes and tubes

Gas-turbine modifications primarily affect the HRSG through a change in exhaust mass flow and temperature. This changes the ratio of HP/IP/LP steam generation as well as overall heat recovery. Many components must be examined for suitable operation. Modifications with high exhaust temperatures may result in excessive desuperheater spray demand as well as superheater and reheater tube metal temperatures above the design temperature.

Avoid ongoing operations that damage the HRSG, including the following:

The desuperheater is responsible for a significant share of damage to superheaters, reheaters, and steam pipes. In some cases, very few fatigue events are needed to initiate tube failures and cracks in the steam piping. There are two underlying causes:

First, there may not be enough energy in the steam to evaporate the spray water. This causes restrained thermal expansion and potentially high stresses in components quenched by the water droplets. The steam temperature downstream of the spray nozzle should be 50 deg F or more above the saturation temperature.

Second, damage to pipes and tubes often occurs when water flows through the spray nozzle without proper atomization. This is caused by a leaking block valve during periods of no spray water demand or from a broken spray nozzle. Water then can flow upstream or downstream through the steam pipe.

A drain pot with automatic detection and drainage is required on all new HRSGs with a desuperheater. In such cases it is important to verify that the drain pot will collect any leakage (sometimes it does not) and is functioning properly.

Burner operation. Excessive heat can damage downstream tubes and duct-wall liner systems. Burner failures result in high localized heat input while faulty control logic can cause a wall of flame pushing through the tube banks.

Burner system controls must be checked as well. Burner output should be controlled to the limitations of the HRSG, not to the burner design maximum. This is especially important when multiple HRSGs have burners controlled to provide a minimum steam generation rate in a common header. If one unit goes offline or if some of the burner elements are isolated, how is the additional heat distributed among remaining units? It is important to verify that controls distribute heat as intended. Burner management system permissives and fuel-skid set points must prevent excessive fuel flow to any one HRSG.

Piping and header drain control. It is critical to verify that low points in the steam pipe and tube circuits are properly drained and that there is no water leakage through steam conditioning systems. If water hammer occurs, it is important to inspect the damage and the position of the pipe. Water hammer could create a low point that did not exist previously. The reheat system can cause extremely expensive pressure-part damage if not maintained and operated properly (including sizing, location, and control).

After shutdown of the HRSG, steam will condense and flow to the lower headers of the HP superheater and the reheater. If this water is not removed prior to startup, steam can push water droplets up tubes or water can restrict steam flow. These conditions cause high stress resulting in tube failures.

HP-drum pressure ramp rate. HP steam drums in cycling service are susceptible to fatigue cracking of nozzles, particularly the downcomers. Exceeding the maximum ramp rate will increase the risk of such cracking.

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501F exhaust-system repairs never ending? Replace to eliminate the problem

Exhaust systems are a presentation and/or discussion topic at most gas-turbine user-group meetings, particularly those supporting F-class and the more advanced frames. Cracking of components, broken struts, material distress, and leaks at joints are almost sure to occur in virtually any system handling a 1000 lb/sec or more of turbine exhaust at 1000F or higher and moving at near mach speed—especially so in starts-based engines with original equipment.

There was a period a few years back when the accepted “solution” was to have personnel standing by to make repairs during annual—or semiannual—outages. In meeting after meeting, discussion focused on weld material, weld configuration, welder qualifications, expansion joints, and related topics. It came to be that users able to restrict repairs to every other outage were recognized for their acumen by peers.

The effects of hot gasses leaking from cracks into areas where they could cause accelerated wear and tear and/or personnel hazards provided owner/operators the incentive to press for root cause analyses and resolve the problems through better design and materials selection. There was a lot of finger-pointing to be sure, mostly directed at the gas-turbine OEMs. However, that might not have been entirely fair given the limited industry experience available to guide the design of early F-class units.

The OEMs of record—Siemens Energy Inc and Mitsubishi Hitachi Power Systems Americas Inc—upgraded the designs of their exhaust cylinders and manifolds for the 501F series of engines to eliminate the issues experienced. These have been retrofitted at several plants, as discussed in some CCJ articles published over the last several years. They can be accessed by using the search function on the magazine’s home page at

More recently, Ansaldo Energia Group’s PSM, headquartered in Jupiter, Fla, has expanded its 501F aftermarket product line to include exhaust systems. The first complete PSM exhaust systems were retrofitted in NV Energy’s Silverhawk Generating Station (Unit B) and Walter M Higgins Generating Station (Unit 2) prior to the 2017 summer run.

Both plants, which began commercial operation in 2004, are 2 × 1 combined cycles powered by Siemens 501FD2 gas turbines. The utility plans to replace the exhaust systems on Silverhawk Unit A and on Higgins Unit 1 during their next major outages—provided upcoming inspections/evaluations confirm expected performance.

Background. The 501F exhaust system has two principal components: an exhaust cylinder, connected to the turbine case on its inlet side and to the exhaust manifold on its outlet side (drawing). The cylinder may be of single- or two-piece construction. PSM’s “drop-in” replacement is a horizontally split two-piece cylinder, the only option available for pre-501FD3 machines when they were purchased. This configuration typically is preferred by users because they can maintain their current maintenance practices in future outages.

Depending on component dimensions, a spacer piece may be required downstream of the exhaust manifold to fit up with the heat-recovery steam generator. An expansion joint is located at the round-to-square transition between the manifold or spacer and the HRSG. In the case of a simple-cycle unit, there would be no HRSG and the manifold or spacer would connect via an expansion joint to the transition piece directing exhaust gas to the stack.

Scott Amos, a gas-turbine subject matter expert in NV Energy’s central engineering group, and Fatima Bouzidi, maintenance manager at Silverhawk, walked the editors through the 501F exhaust-system challenges their company faced—including the following:

    • Failure of static seals, allowing hot exhaust to contact bearing support struts, causing overheating and cracking which allowed the aft bearing and rotor to “drop.” The rotor drop reduced critical compressor and turbine radial clearances to the point where metal-to-metal contact between the casing and rotating components became a concern. Experience of other users is that a crack can propagate quickly, extend through the entire strut, and force the unit into an outage with extensive damage.

    • Thus timely strut repair and clearance correction are recommended to prevent the possibility of a wreck. Repairs and realignment are expensive undertakings, to be sure. Remember, too, that access to the aft bearing for inspection and the taking of measurements on legacy equipment is not a simple matter. In NV Energy’s experience, it takes about a day and a half to cool an exhaust system with compromised seals before you can drop down through the manway and crawl forward to the bearing.

    • No end to the cracking/repair cycle experienced with the exhaust cylinder. This was due, in part, to failure of baffle plates, allowing recirculation of exhaust gas to the dead-air space. PSM’s “fix” prevents recirculation and the casing creep issues attributed to it.

Exhaust gas also can overheat expansion joints, allowing them to leak and create safety and environmental issues. Repairs are time-consuming and expensive, and never “final.”

NV Energy’s engineering team had been following industry experience on 501F exhaust systems for years, while continually evaluating the condition of its Silverhawk and Higgins units, before deciding on a course of action for its assets. Amos said after receiving multiple alerts from the OEM and listening to owner/operator colleagues at forums such as the 501F Users Group (next meeting Feb 17-22, 2019 in Paradise Valley, Ariz), it was obvious that repairs are temporary and the only long-term fix is replacement of the exhaust cylinder.

Bearing drops on the four 501Fs at Higgins and Silverhawk were monitored by PSM. The relatively constant drop in rotor centerline position of Higgins 2 over time averaged about 10 mils annually. Silverhawk B experienced a more severe drop: about 15 mils per year on average.

With the future easy to predict, NV Energy engineers conducted detailed design reviews of replacement exhaust systems offered by the two OEMs and PSM. The company focused on reliability improvements and reduced maintenance promised by the offerings. Its goals were the following:

    • Eliminate exhaust-bearing drop.

    • Improve the low-cycle fatigue life of the cylinder and its struts.

    • Improve system durability in all modes of operation, with a focus on cycling.

    • Reduce the thermal constraint on the strut shield.

    • Improve the exhaust-cylinder/HRSG connection and protect the HRSG inlet expansion joint.

    • Provide better access to areas that may require repairs.

    • Assure compatibility with the existing structure, piping, and other connections.

Major design changes by PSM (from the original exhaust system) to achieve the goals bulleted above were these:

    • Change exhaust-bearing support struts from Type-410 stainless steel to a nickel-based super alloy.

    • Redesign exhaust cylinder and manifold support structure, and improve aerodynamics.

    • Eliminate baffle seals by integrating a new manifold front flange into all PSM exhaust installations.

    • Reduce thermal stress by making changes to material geometry.

    • Change diffuser and strut shield to Type-347 stainless steel from Hastelloy®.

    • Redesign exhaust-cylinder and -manifold gas-path seals.

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INDUSTRY NOTES, November 2018

Registration opens for three 2019 user meetings; sign up now and make good use of your 2018 budget surplus

In the last couple of weeks, registration opened for three high-profile 2019 conferences dedicated to the information needs of owner/operators: 501F Users Group, Western Turbine Users Inc, and HRSG Forum with Bob Anderson. The details provided below are intended to encourage your participation.

501F Users Group

Dates: February 17 – 22
Location: Paradise Valley (Scottsdale), Ariz
Venue: DoubleTree Resort by Hilton

The compelling program for this meeting will be posted online shortly. It will have many of the same elements as the information-rich 2018 conference, which ran four days and included the following:

    • User presentations on issues identified in the fleet and solutions implemented, as well as on experience with upgrades to improve unit performance.

    • User-only sessions promoting open discussions and short presentations by owner/operators on safety; compressor, combustion, hot-gas, inlet, and exhaust sections; rotors; auxiliaries; and generator.

    • Special closed sessions, ranging from two to four hours each, by the major products/services providers serving this frame: Siemens, Mitsubishi, Ansaldo Energia’s PSM, and GE.

    • Vendorama progam. At the meeting last February, 33 companies made 35 half-hour technical presentations to bring attendees up to date on products/services of interest to the 501F community.

    • Vendor fair, following the Vendorama program on the first day of the meeting, gives users the opportunity to peruse the offerings of nearly a hundred manufacturers and services firms.

If you have never attended a 501F Users Group meeting, make the 2019 conference your first. You will learn things vital to your plant’s future success that’s not available in one place anywhere else.

Western Turbine Users Inc

Dates: March 17 – 20
Location: Las Vegas, Nev
Venue: South Point Hotel & Spa

GE aero (LM2500, LM5000, LM6000, and LMS100) owner/operators from around the world will share experiences, both good and bad, at the 29th annual meeting of the Western Turbine Users. Get all the details at the group’s well organized, easy-to-navigate website—social events, agenda, special tours, exhibit hall, breakout sessions, etc. Then register and book your hotel room at the same website for the electric-power industry’s largest independent user group meeting. 

HRSG Forum with Bob Anderson

Dates: July 22 – July 25
Location: Orlando, Fla
Venue: Hilton Orlando

With two solid events under its belt, the HRSG Forum with Bob Anderson introduces an expanded program for the organization’s third annual conference and exhibition (diagram), making it the undisputed king of content in the world of heat-recovery steam generators. HRSG Week 2018 begins with a Make-up Water Workshop (July 22) the day before the traditional two-day HRSG Forum and concludes with the morning session of EPRI Technology Transfer Day (July 25).

You can register for the entire program now for only $650; or $475 for the two-day forum plus the EPRI session on Thursday morning. The user-driven program features technical presentations by HRSG experts, with significant time for group discussions and networking with peers. Plus, registrants will receive complete meeting minutes, copies of presentation slides, and up to 24 hours of continuing education units (forum + workshop + technology day).

Visit the website periodically for program details as they become available.

Ring eight bells for Frank Berté, 77

News of Dr Frank Berté’s passing on July 4, 2018 reached us only recently. He was the co-founder of Tetra Engineering Group Inc, perhaps known best by readers of CCJ for its solutions to problems associated with heat-recovery steam generators and high-energy piping systems.

Berté was a frequent participant at user group vendor fairs and an occasional presenter. He was easily distinguishable among the many exhibitors because of his calm, quiet nature in a sea of salespeople. Plus, he never arranged his table display without his funky air-powered simulated flame. You could spot him “a mile away.”

Peter S Jackson, PE, who succeeded Berté as president of Tetra, remembers Frank as an excellent engineer, inspiring leader, and genuinely friendly man. Everyone who knew Frank or worked with him, Jackson said, enjoyed his enthusiasm for work and love of life.

Berté’s career in the electric power industry spanned nearly five decades; it began in the mechanical engineering group at Commonwealth Edison Co’s Dresden Generating Station. Next step was a management position in the reactor design department at Combustion Engineering Inc. Berté founded Tetra with two other engineers in 1989.

Later he started Innovative Marine Technology to pursue, in his spare time, the design of sailboats and other things related to the sea. Accomplishments included the first ever Tridactyl sailboat, which he patented. Also, TankerProa, a modular sailing vessel using Tridactyl technology to help power transoceanic tankers.

Berté was a restless doer who kept his hands and mind moving non-stop—always receptive to professional challenges and to sharing his knowledge with industry colleagues. One example of the latter was an article he penned for the first issue of CCJ, “Assessing the true cost of cycling operation is a challenging assignment.” Things haven’t changed much on this in the 15 years since its publication.

Born in Brooklyn, Frank moved to the Bronx with his family before continuing his migration north to West Hartford, Conn, and later to Westford, Mass. He earned a Master’s Degree in Mechanical Engineering from The City College of New York and a PhD in Nuclear Engineering from the Massachusetts Institute of Technology.

IAPWS working group reports progress on four new documents

The Power Cycle Chemistry (PCC) working group of the International Association for the Properties of Water and Steam gathered at the parent organization’s annual meeting in Prague, Czech Republic, Sept 2-7, 2018, to advance the development of several new Technical Guidance Documents (TGDs).

The annual IAPWS (pronounced eye-apps) conference was conducted concurrently with the International Conference on the Properties of Water and Steam (ICPWS), which is held every four or five years. The 2018 edition of the ICPWS was the seventeenth; the first was held in London in 1929.

The joint meeting attracted more than 100 papers from 140 scientists and engineers representing 27 countries. Purpose of the conference is to connect scientists with the engineers who use their information. Both groups of professionals benefit: The researchers/scientists learn about problems seeking resolution while the engineers gain access to the latest research results. The information exchange included experience with film-forming substances (FFS), which are of increasing interest to combined-cycle owner/operators.

IAPWS Executive Secretary Dr R Barry Dooley of Structural Integrity Associates Inc, well known to the global power-generation community, contacted CCJ’s editorial offices to say that four TGDs are in final draft form with planned release dates in 2019:

    • Guidance on air in-leakage.

    • Guidance on the use of FFS in industrial plants.

    • Guidance on generator-cooling-system chemistry.

    • Guidance for ensuring the integrity and reliability of demineralized makeup water supply.

Additionally, the PCC working group is preparing several white papers likely to be developed into TGDs at a later time. These include “Corrosion Products in Flexible (cycling, two-shifting) Plants” and “Guidance for HRSG Condensate Polishing Plants.”

Dooley reminded that there are eight TGDs currently available free-of-charge on the organization’s website at They offer a wealth of practical information on topics such as steam purity for turbine operation, phosphate and sodium hydroxide treatments for steam/water circuits of drum-type boilers, instrumentation for monitoring cycle chemistry, how to measure carryover of boiler water into steam, etc.

The next IAPWS meeting will be held in Banff, Canada, Sept 29-October 4, 2019.

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Factor European experience into O&M practices at US combined cycles, Part I

European Technology Development Ltd’s (ETD Consulting), International Conference on Power Plant Operation and Flexibility, held in London in July 2018, covered recent developments in plant materials, operation, inspection, maintenance, and costs related to both baseload and cycling operation for different types of plants—including combined cycles. Participants included plant owners/operators, consultants, researchers, manufacturers, and inspection-agency professionals.

Conference organizer Dr Ahmed Shibli, managing director of ETD Consulting, pointed to the following global trends:

    • Europe is going through the same market changes as North America. Cycling is global.

    • Some countries have more cycling and low-load experience than North America—such as those with geothermal and hydroelectric plants that cause varied operation of fuel-fired assets. This experience base has wide-ranging value.

    • Europe and Japan are taking active roles in high-temperature materials development and testing.

Shibli’s primary purpose in arranging the meeting was to help identify the basic causes of equipment problems in both baseload and cycling units, and to clarify modifications, inspections, and procedures that will minimize costs.

Who wins when plant components fail? A question asked by one of the first speakers, David Allen of Impact PowerTech Ltd (UK), “Who wins when plant components fail?” set the tone for the conference and was the perfect segue for his presentation on the upgrading of materials and welds. Allen’s next question was equally pointed: “Why do we so often stick with last-century technology?”

The speaker began with a philosophical look at planned obsolescence. He cited interesting examples from the automobile, white goods, and communications industries. Participants were captivated, and on alert for more.

Allen did not claim current evidence of planned obsolescence within the power industry, and in fact stated that a manufacturer with a unique design is careful to maintain its good reputation.

But he did note some dangers similar to those expressed by Eskom (South Africa) at last year’s Air-Cooled Condenser Users Group meeting in Las Vegas. To wit, we all experience the ongoing pressures for low bids, rapid investment payback, and increasingly stringent trading conditions.

The potential menace is commonly applied standards that fail to ensure the most reliable long-term component operation. In other words, once a supplier meets the standards or codes in the specification, further refinements or improvements can become less important (and more expensive) to the supplier. The same is true on qualifying bids for component supply. Providers’ reputations are at less risk as long as they meet the qualifications.

Perhaps because “innovation brings risk,” or because “regular repair and maintenance activities provide jobs,” we could be letting ourselves down, suggested Allen. And in his words, “We are still building new plants with 40-year-old materials (P91, Alloy 617) and ignoring the newer, potentially better alternatives.”

And how has market-driven flexible operation changed things? “Cycling makes it worse!”

Details have become clear, stressed Allen:

    • Flexible operation only makes service exposure more onerous.

    • Thermomechanical transients cause additional cyclic loading, which is conducive to the following: 1. Mechanical and thermal fatigue cracking, 2. Creep-fatigue cracking (with creep ductility exhaustion attributed to repeated transient creep strain), and 3. Creep cracking (with creep life reduction caused by increased loading).

    • Poor temperature control can severely shorten creep life.

    • Creep issues do not go away; they get much worse.

    • Fatigue brings additional challenges.

    • Sticking with last-century technology increases risk!

So how do owners/operators minimize the potential costs? Allen outlined some thoughts:

  1. 1. Design out “at-risk features” (thickness and materials mismatches, closely spaced header stubs, dissimilar-metal welds, etc).

  1. 2. Improve temperature control during startups and transients.

  2. 3. Make components thinner—perhaps.

    • Thinner components minimize thermal/mechanical mismatch loading and may therefore perform better when fatigue is a problem.

    • But thinner components will experience higher pressure stresses and may therefore perform worse when creep is a problem.

Allen reviewed typical owner/operator options. Some choose to continue operation until plant end-of-life, mindful primarily of safety. Many take the financial hit and accept high inspection, repair, and replacement costs. The better strategy is to install upgraded retrofit components with stronger materials and welds at the same thickness (better for creep) or thinner (better for fatigue).

He then presented details and examples of current P92 materials with good-quality heat treatment, labeling this “a materials upgrade solution that is ready now.” Following in-depth discussions of various manufacturing methods, heats, ductility, and tensile strength, he asked participants to “Stop fearing P92!” 

And he gave specifics from a recent review, showing a “strong correlation between heat treatment and ductility.” He concluded that “normalizing is about twice as important as tempering. Under-normalizing is the main problem. Under-tempering makes the problem worse.” And “notably, normalizing time is more important than temperature.”

    • The four most creep-brittle casts, with long-term average area reduction (Ra) in creep test values in the range of 3% to 12%, all had normalizing times in the range of 0.2 to 0.6 hours.

    • The seven next most creep-brittle casts, all with Ra values in the range of 18% to 24%, had normalizing times of 0.2 to 1.0 hours.

    • No cast with a normalizing equivalent to 2 hours at 1050C or 1 hour at 1070C had a long-term Ra value lower than 28%.

Summary: This indicates that simple controls on allowable heat treatment can resolve the Grade 92 creep brittleness concern. Further work is ongoing to assess very long-term ductility out to 100,000 hours, and beyond.

Allen next looked at “near-future MarBN, a novel high-alloy steel for powerplants.” This material, being studied primarily in Japan and the UK, is martensite plus boron and nitrogen. The process involves “careful microalloying with boron and limited nitrogen for high creep strength.” Allen listed temperature capability of P92 as about 20 deg C better than P91 and “expects temperature capability of MarBN to be at least 25 deg C better than P92.”

But the microalloying process is extremely sensitive.

Following discussions on welding processes, he offered the following conclusions:

  1. 1. “Today we can replace P91 with P92.

  2. 2. Tomorrow we could use MarBN for even greater security.”

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