News & View, Volume 47 | Surface Preparation – A Pivotal Step in the Inspection Process

News & View, Volume 47 | Surface Preparation – A Pivotal Step in the Inspection Process

By:  Ben Ruchte, Steve Gressler, and Clark McDonaldNews & View, Volume 47 | Surface Preparation – A Pivotal Step in the Inspection Process

Properly inspecting plant piping and components for service damage is an integral part of proper asset management.  High energy systems constructed in accordance with ASME codes require appropriate inspections that are based on established industry practices, such as implementation of complimentary and non-destructive examination (NDE) methods that are best suited for detecting the types of damage expected within the system.  In any instance where NDE is used to target service damage, it is desirable to perform high quality inspections while at the same time optimizing inspection efficiency in light of the need to return the unit to service.  This concept is universally applicable to high energy piping, tubing, headers, valves, turbines, and various other power and industrial systems and components.

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News & View, Volume 47 | Metallurgical Lab Case Study- Corrosion Fatigue in WaterWall Tubes Increasingly A Safety Concern as Coal Plants Cycle

News & Views, Volume 47 | Metallurgical Lab Case Study: Corrosion Fatigue in WaterWall Tubes Increasingly A Safety Concern as Coal Plants Cycle

By:  Ben RuchteNews & View, Volume 47 | Metallurgical Lab Case Study- Corrosion Fatigue in WaterWall Tubes Increasingly A Safety Concern as Coal Plants Cycle

It is well known that conventional coal-fired utility boilers are cycling more today than they ever have.  As these units have shifted to more of an ‘on-call’ demand they experience many more cycles (start-ups and shutdowns, and/or significant load swings) making other damage mechanisms such as fatigue or other related mechanisms a concern. 

The most recent short-term energy outlook provided by the U.S. Energy Information Administration (EIA) indicates the share of electricity generation from coal will average 25% in 2019 and 23% in 2020, down from 27% in 2018.  While the industry shifts towards new construction of flexible operating units, some of the safety issues that have been prevalent in the past are fading from memory.  The inherent risks  of aging seam-welded failures and waterwall tube cold-side corrosion fatigue failures are a case in point.   It is well known that conventional coal-fired utility boilers are cycling more today than they ever have.  As these units have shifted to more of an ‘on-call’ demand they experience many more cycles (start-ups and shutdowns, and/or significant load swings) making other damage mechanisms such as fatigue or other related mechanisms a concern.  The following case study highlights this point by investigating a cold-side waterwall failure that experienced Corrosion Fatigue.  While this failure did not lead to any injuries, it must be stressed that the potential for injuries is significant if the failure occurs on the cold-side of the tubes (towards the furnace wall).

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News & View, Volume 47 | Materials Lab Featured Damage Mechanism- SH:RH Fireside Corrosion in Conventional Coal Fired Boilers

News & Views, Volume 47 | Materials Lab Featured Damage Mechanism: SH/RH Fireside Corrosion in Conventional Coal Fired Boilers

By:  Wendy Weiss

Superheater/reheater fireside corrosion is also known as coal ash corrosion in coal fired units.

News & View, Volume 47 | Materials Lab Featured Damage Mechanism- SH:RH Fireside Corrosion in Conventional Coal Fired Boilers

MECHANISM
Coal ash corrosion generally occurs as the result of the formation of low melting point, liquid phase, alkali-iron trisulfates. During coal combustion, minerals in the coal are exposed to high temperatures, causing release of volatile alkali compounds and sulfur oxides. Coal-ash corrosion occurs when flyash deposits on metal surfaces in the temperature range of 1025 to 1200oF. With time, the volatile alkali compounds and sulfur compounds condense on the flyash and react with it to form complex alkali sulfates such as K3Fe(SO4)3 and Na3Fe(SO4)3 at the metal/deposit interface, which are low melting point compounds. The molten slag fluxes the protective iron oxide covering the tube, exposing the metal beneath to accelerated oxidation.

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News & View, Volume 46 | Metallurgical Lab Featured Damage Mechanism- Waterwall Fireside Corrosion (WFSC) in Conventional Boilers

News & Views, Volume 46 | Metallurgical Lab Featured Damage Mechanism: Waterwall Fireside Corrosion (WFSC) in Conventional Boilers

By: Wendy Weiss

News & View, Volume 46 | Metallurgical Lab Featured Damage Mechanism- Waterwall Fireside Corrosion (WFSC) in Conventional BoilersIndustry experience shows that waterwall tubing in conventional boilers can be susceptible to fireside corrosion, depending on fuel type, firing practice, etc. In boilers where fireside corrosion has been identified as a maintenance issue, wastage rates of 5 to 25 mils/year are not uncommon. Since the mid 1990s, the installation of low NOx burner systems designed to lower NOx emissions has significantly increased the wastage rates in some boilers. Operators of subcritical boilers have reported wastage rates as high as 30 mils/year, while those operating supercritical boilers have reported rates exceeding 100 mils/year in the worst cases. These higher damage rates have resulted in an increase in tube failures, and operators have struggled to accurately define the extent of the damage and install the appropriate mitigating technologies.

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News & View, Volume 46 | Plant Integrity Assistant – There’s an App for That! PlantTrack App Now Available

News & Views, Volume 46 | Plant Integrity Assistant – There’s an App for That!

By:  Matt Freeman

PlantTrack App now available

News & View, Volume 46 | Plant Integrity Assistant – There’s an App for That! PlantTrack App Now AvailablePlant engineers must often answer ‘what damage is this piece of equipment susceptible to, and what can we do about it?’ or ‘how much longer can this component continue operating’?   A free app is now available in both the Google Play store and the Apple App store to help answer these and other equipment integrity questions (see figure 1).

The PlantTrack App is a plant integrity assistant that provides life calculators, damage mechanism guides, technical articles, lab sample submittal form, and other functions relevant for plant engineers.  While it is geared towards fossil (both coal and gas) power plants, it has applicability for equipment at other plants as well.  For subscribers to the PlantTrack web application, the mobile app also provides a dashboard view of inspection history, action items, damage tracking results, etc.  Users of the PlantTrack software will recognize some of the features from the ‘PlantTrack Tools’ that have previously been available through a web browser.

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News & View, Volume 45 | Life Management for High Energy Piping (HEP)

News & Views, Volume 45 | Life Management for High Energy Piping (HEP)

By:  Matt Freeman

News & View, Volume 45 | Life Management for High Energy Piping (HEP)High Energy Piping systems, including main steam and hot reheat piping, are typically very reliable and can often operate trouble-free for decades.  However, due to the combination of pressure and temperature at which such systems operate, a failure can have catastrophic consequences from a safety perspective and in terms of equipment loss.  Because of this and the requirements of the ASME B31.1 Power Piping code, HEP programs – or as defined by Code, Covered Piping Systems (CPS) – are established to ensure that the integrity of the system is maintained throughout their lifecycle.  This article discusses the steps required to implement an HEP / CPS life management program.

A Life Management Program is not synonymous with an inspection program.  Inspections are an important part of an overall program but should be complimentary to the use of analytical tools, real-time monitoring, and laboratory examinations

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News & View, Volume 45 | The Importance of HRSG HP Evaporator Tube Internal Deposit Evaluation

News & Views, Volume 45 | The Importance of HRSG HP Evaporator Tube Internal Deposit Evaluation

By:  Barry Dooley

News & View, Volume 45 | The Importance of HRSG HP Evaporator Tube Internal Deposit EvaluationEvaluation of High Pressure (HP) Evaporator Tube Deposits is important for several reasons:

  • Determining if flow-accelerated corrosion (FAC) might be occurring in the lower pressure circuits.
  • Regular evaluations can provide information on the internal deposit deposition rate, which is information necessary to help prevent under-deposit corrosion damage mechanisms.
  • Provides information necessary to develop an optimized cycle chemistry for HRSGs.
  • Can help determine if the HRSG needs to be chemically cleaned.

The leading heat recovery steam generator (HRSG) tube failure mechanisms are FAC, thermal and corrosion fatigue, and under-deposit corrosion (UDC) and pitting. The corrosion products released by the FAC mechanism are transported from the affected area (typically the feedwater or lower pressure systems) and can eventually reach the HP evaporator tubing, so understanding the deposition in the HP evaporator is an important step in determining if FAC might be occurring. Deposition on the inside of HP evaporator tubing is also a precursor to any of the under-deposit corrosion HRSG tube failure mechanisms.

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News & View, Volume 44 | Real-Time Damage Tracking with SI Technology and GP Strategies’ EtaPro Expanding Capabilities in Condition-based Pressure-part Integrity Management

News & Views, Volume 44 | Real-Time Damage Tracking with SI Technology and GP Strategies’ EtaPro

By:  Matt Freeman

Expanding Capabilities in Condition-based Pressure-part Integrity Management

News & View, Volume 44 | Real-Time Damage Tracking with SI Technology and GP Strategies’ EtaPro Expanding Capabilities in Condition-based Pressure-part Integrity ManagementStructural Integrity and GP Strategies recently announced an agreement to bring SI’s technology for calculating, tracking, and trending life consumption of piping and boiler components to GP Strategies EtaPRO real-time monitoring platform (Press release here).  SI has a long history with creep and fatigue damage monitoring applications, most recently with the suite of applications available as part of SI’s PlantTrack platform.  The partnership with GP Strategies brings that technology to EtaPRO, which is used worldwide by power-generating organizations to monitor the performance and reliability of their generation assets.

EtaPRO users will benefit from easy integration of SI’s leading-edge Boiler and Piping Component Reliability (BPCR) modules to quantify damage to high-pressure, high-temperature components such as tubing, piping, headers, and desuperheaters. The BPCR modules track and trend accumulated creep and fatigue damage in real time using SI’s proprietary algorithms that combine actual operating data and material condition with a plant’s specific configuration. Plant operators can use the resulting life consumption estimates to guide asset management decisions, such as changes in operating procedures, targeted inspections, or off-line analysis of anomalous conditions.

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News & View, Volume 43 | Attemperator Damage Prevention A Case Study Using Online Monitoring

News & Views, Volume 43 | Attemperator Damage Prevention A Case Study Using Online Monitoring

By:  Fred DeGrooth and Ulrich Woerz

News & View, Volume 43 | Attemperator Damage Prevention A Case Study Using Online MonitoringAttemperators (aka desuperheaters) are used in fossil and combined cycle plants to protect boiler/HRSG components and steam turbines from temperature transients that occur during startup or load changes. The attemperator sprays water droplets into the superheated steam to ensure that the downstream, mixed, steam temperature will not adversely affect downstream components.  While there are a number of attemperator designs and configurations (Figure 1 shows a schematic of a typical arrangement), all of them are potentially vulnerable to damage, making attemperators one of the most problematic components – particularly in combined cycle plants. If the causes of damage are not identified (and addressed) early, then cracking and steam leaks can occur leading to costly repairs and replacements. 

The frequent cycling and wide operating range of combined cycle plants impose particular demands on attemperator functionality.  Spraywater demand to the attemperator can fluctuate greatly within a startup where heat input to the boiler and steam flow are changing rapidly.  At part load operation spraywater may be required continuously to moderate steam temperatures because of high exhaust gas temperature from the combustion turbine.  Spraywater may also be demanded when duct burners are fired. 

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News & View, Volume 43 | Metallurgical Lab- Dissimilar Metal Welds (DMW) in Boiler Tubing The need for confirmation- A Case Study

News & Views, Volume 43 | Metallurgical Lab: Dissimilar Metal Welds (DMW) in Boiler Tubing

By:  Tony Studer

The need for confirmation: A Case Study

News & View, Volume 43 | Metallurgical Lab- Dissimilar Metal Welds (DMW) in Boiler Tubing The need for confirmation- A Case StudyAs plants age, the need for inspection for service related damage to ensure unit reliability increases. There are several approaches that plants can take to reduce the risk of premature failures and proactively manage their DMWs. First is metallurgical sampling. Based on temperature profiles across the boiler, operating conditions, and operating history, DMWs can be selected for laboratory analysis. This will provide some insight into possible damage accumulation; however, the better approach, if damage is suspected, is to perform an ultrasonic inspection of the DMWs. This allows inspection of all the DMWs, and only requires access and surface preparation. If indications are detected, then tube sampling should be performed. It is critical to perform a metallurgical analysis of several of the DMWs suspected of containing service damage to confirm that the indications are service related and to help establish the extent of the damage compared to ultrasonic testing results. Typical DMW damage is described in the Featured Damage Mechanism article. The importance of the metallurgical analysis is demonstrated in the three following case studies.

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