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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

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

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)

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

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

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

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.

CFD Analysis of failed 180° Bend, 2013
Middle East

CFD Analysis of failed 180° Bend, 2013

A CFD study on one of the 4th quadrant pipe bends at a thermal power plant steam boiler was performed. The purpose of the analysis was to analyse the change in flow velocity due to an increase in the bend nominal size from 3” to 4”. The connecting pipe run was kept at 3” and standard expander/reducers are used to join the pipe with the bend. Input process parameters were taken from a PPSD model.

LP Economiser Header Failure Analysis, 2010
Middle East

LP Economiser Header Failure Analysis, 2010

The LP economiser lower header on a HRSG ruptured shortly after a diverter damper incident. Tetra was approached by the client to investigate the possible root causes for the rupture. The unit went into single element control at the time of the incident and the LCV cycled through fully open / fully closed positions to maintain the drum level after “shrink”. When the damper re-opened the LCV remained closed as the drum level increased (swell). The economizer temperature increased and there was an associated increase in pressure. The safety valve failed to operate as it was accidentally gagged, causing serious over pressurisation and a burst header.

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