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Guides techniques

Tetra a publié une série de guides qui peuvent être commandés.

HRSG Inspection Planning Guide (2nd Edition)

Inspection is part of routine maintenance for any Heat Recovery Steam Generator (HRSG). Visual inspections are performed at regular intervals in accordance with the requirements of regulatory bodies and insurers.

HRSG Tube Failure Diagnostic Guide (3rd Edition)

Heat Recovery Steam Generator (HRSG) tubes provide the media for extraction of useful energy from the waste heat in gas turbine exhaust at combined cycle power plants (GT-CCs) or from heat generated by process streams at petrochemical facilities.

Article Techniques

Une sélection de documents techniques disponibles à titre de référence.

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Creep Classification of Grade 91 Steel

Background Grade 91 steel is superior to many other industry used materials for its increased resistance to m...

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Power Boiler Piping

Boiler piping design requirements is divided into internal and external jurisdictions. These are divided...

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Welding Procedure Specification (WPS)

Before any welding activity can commence, the welder and the QC Engineer has to be fully aware of the content ...

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Water Chemistry in HRSGs

The environment on the inside of HRSG tubing is an important factor in maintaining tube integrity. The c...

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HRSG Inspection Planning

Building a good inspection plan for the HRSG involves doing the following: Set the Time and General Schedul...

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Tube Failures related to Water Chemistry

Most corrosion induced tube failures have a component that is directly related to water chemistry. The c...

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Articles, présentations et articles

Sélection d'articles, de présentations et d'articles issus de conférences et d'événements majeurs de l'industrie.

Title
Author
Chemical Cleaning of HRSGs: When, Where and How?
Chemical Cleaning of HRSGs: When, Where and How?Chemical Cleaning of HRSGs: When, Where and How?
Malloy J.
European HRSG Forum, Munich, 2015.
Role of Boiling Mode and Rate in Formation of Waterside Deposits in Heat Recovery Steam Generator Evaporator Tubes
Role of Boiling Mode and Rate in Formation of Waterside Deposits in Heat Recovery Steam Generator Evaporator TubesRole of Boiling Mode and Rate in Formation of Waterside Deposits in Heat Recovery Steam Generator Evaporator Tubes
Moelling D., Malloy J.
ASME POWER 2014 Conference, July, 2014.
Evaluating Contributions of Flow-Accelerated Corrosion and Liquid Droplet Impingement to Pipe Thinning in HRSG Evaporator Tubes
Evaluating Contributions of Flow-Accelerated Corrosion and Liquid Droplet Impingement to Pipe Thinning in HRSG Evaporator TubesEvaluating Contributions of Flow-Accelerated Corrosion and Liquid Droplet Impingement to Pipe Thinning in HRSG Evaporator Tubes
Malloy J., Graham M., Taylor M., Fabricius A., Moelling D.
EdF FAC Conference Avignon, May 2013 and Power Plant Chemistry 2013
Design factors for avoiding FAC erosion in HRSG low-pressure evaporators
Design factors for avoiding FAC erosion in HRSG low-pressure evaporatorsDesign factors for avoiding FAC erosion in HRSG low-pressure evaporators
Malloy J., Taylor M., Fabricius A., Graham M., Moelling D.
July 2013, ASME POWER Conference, USA
Ten Year Retrospective Look at HRSG FAC Assessment and Incidence
Ten Year Retrospective Look at HRSG FAC Assessment and IncidenceTen Year Retrospective Look at HRSG FAC Assessment and Incidence
P.S. Jackson, D.S. Moelling, M.J. Taylor (Tetra)
Jul 1, 2010, Fossil FAC International Conference, USA

Projets Récents

Avec plus de 30 ans d'expérience dans les services de production d'électricité et de vapeur industrielle, Tetra Engineering a une longue histoire de projets.

Europe

Root Cause Analysis of HP Drum Nozzle Cracking, 2018

During the 2018 shutdown at a CCGT in Europe several of the HRSG HP drum riser nozzle and downcomer nozzle welds were checked and all were found to be cracked on the inside of the drum, at the weld toe or between weld beads, with the cracks following the fusion line back to the nozzle. The drum feedwater inlet and steam outlet nozzles (above drum waterline) were both undamaged. The drums were removed and all welds were repaired in the workshops. Tetra performed Finite Element Analysis (FEA) and operational data analysis and could conclude that the operational stresses were high enough given the current cycling regime to cause the cracking observed. The quality and design of the original welds is also likely to have contributed to the cracking.

Middle East

Diverter Damper Design & Operation Review, 2018

Tetra was engaged by a client to investigate the recently observed cracking on the diverter damper actuator. The design documentation and failure mode was reviewed. From this initial review it could be concluded that the shaft cracking is most likely a result of the operating procedure, where  the damper is kept in an open position for an extended period of time. The exposure to hot flue gas in combination with the load acting on the toggle arms is the most likely source of the cracking

South East Asia

Flow Accelerated Corrosion Risk Assessment, 2017

An assessment of the susceptibility of HRSG piping components was performed according to Tetra Engineering’s FACRisk™ methodology which includes the use of thermal modelling simulation software (PPSD). From each system, sub groups are ranked using both time to minimum wall thickness and wear rate. The highest risk components (such as elbows, tees and valves) are identified. Overall, due to relatively high operating pH level (>9.2), the overall risk of FAC failures at the CCGT plant in question was considered to be relatively low, with few specific areas showing increased risk. Three separate load cases were simulated and analysed to determine the potential FAC risk. The results of each simulation were incorporated into the final locations recommended for inspection.

Asia

Boiler Tube Failure Root Cause Analysis, 2017

After several tube failures in recent years in the 1st row of LTRH hanger tubes, Tetra was tasked with performing a Root Cause Analysis (RCA) to determine the underlying cause of the failures. A detailed review of operating data, failure reports and design information was carried out and potential causes investigated. The tube failure mechanism as determined by metallurgy was short-term overheating, with temperatures likely exceeding 700°C prior to failures. Two contributing causes were identified by elimination of all other possibilities: temporary loss of steam flow in affected leading row tubes coupled with high flue gas temperatures in certain tubes at the side of the boiler gas path.  Unfortunately, the underlying root cause of the loss of flow could not be confirmed, whereas the asymmetric flue gas temperature distribution is a known issue since commissioning.

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