Resources

Consult our range of free resources.

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Technical Guides

Tetra has published a series of guides which are available for ordering.

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.

Technical White Papers

A selection of technical papers available for reference.

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Gas side Layup

Gas side Layup

Gas-side corrosion occurs during shutdown. It is highest in the cold-end tube sections because of the pr...

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HRSG Preservation

HRSG Preservation

The preservation of the HRSG fluid and steam systems during shutdown periods is an important objective at any ...

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Tube Failures related to Layup

Tube Failures related to Layup

Oxygen is a common contaminant in the boiler water that is particularly corrosive to carbon steel. Many ...

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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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Water Side Layup

Water Side Layup

The primary reason for choosing wet layup is that the time to restart the boiler is considerably shorter than ...

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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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To discuss how we might assist you to improve your plant's performance or to maintain its value over time

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Papers, Presentations and Articles

Selected papers, presentations and articles from major industry conferences and events.

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

Previous Projects

With over 30 years of experience in power and industrial steam generation services, Tetra Engineering has along history of projects.

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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