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.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
What do HRSG tube failure statistics tell us?
What do HRSG tube failure statistics tell us?What do HRSG tube failure statistics tell us?
Misha Gadher & Mark Taylor
Modern Power Systems
Counterfeit, Fraudulent and Suspect Items (CFSI) – Steel and HRSGs
Counterfeit, Fraudulent and Suspect Items (CFSI) – Steel and HRSGsCounterfeit, Fraudulent and Suspect Items (CFSI) – Steel and HRSGs
Taylor M.
IMechE HRSG User Group 2022
Adapting Existing Thermal Desalination Plants to Produce Hydrogen
Adapting Existing Thermal Desalination Plants to Produce HydrogenAdapting Existing Thermal Desalination Plants to Produce Hydrogen
Malloy J.
2022 World Utilities Congress
Root Cause Failure Investigation of MSCV Drain Failures
Root Cause Failure Investigation of MSCV Drain FailuresRoot Cause Failure Investigation of MSCV Drain Failures
P. Jackson, A. Wholey, E. Tsai and D. Burns
ASME 2022 Pressure Vessels & Piping Conference
Predicting and Preventing Risk of Vibration Induced Failures in Boilers and Heat Recovery Steam Generators (HRSG)
Predicting and Preventing Risk of Vibration Induced Failures in Boilers and Heat Recovery Steam Generators (HRSG)Predicting and Preventing Risk of Vibration Induced Failures in Boilers and Heat Recovery Steam Generators (HRSG)
Fabricius A., Malloy J., Taylor M., Moelling D.
Proceedings of the ASME 2022 Power Conference

Previous Projects

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

HRSG Boiler Preservation Study, 2014
Middle East

HRSG Boiler Preservation Study, 2014

A CCGT power plant employed Tetra to perform a review of possible boiler preservation options within the context of the present and planned operating regime. The review relied on information supplied by the plant staff, Tetra field experience and latest industry trends and practices to identify the most promising strategy for preservation. The ideal solution for this client was Dry Layup that is systematically applied when it reaches the end of the standby period. This would require that resulting startup timing meets requirements imposed by the governing network operator.

Thermohydraulic Attemperator Study using PPS&D, 2014
Europe

Thermohydraulic Attemperator Study using PPS&D, 2014

The primary purpose of this study was to validate the effect of an interstage attemperator between two superheaters with respect to the primary superheater and primary reheater outlet steam temperatures. The CCGT in question had already had problems with creep failures of the P91 components, and needed to assure that exit temperatures did not exceed 570°C. Currently, the primary superheater outlet temperatures exceed 600°C at certain loads and the primary reheater temperatures exceed 590°C. Initial results were based on steady-state analysis, while final results included dynamic modeling of cold-, warm- and hot starts, as well as ramp up and ramp down. The study was performed using the software simulation tool PPS&D.

Stress Analysis Study of SH Section, 2014
South East Asia

Stress Analysis Study of SH Section, 2014

A CCGT Power Plant suffered repeated tube failures between 2003 and 2014 in the SH section of their boiler. Failures were exclusively located at the tube-header weld, at varying positions on the tube sheet. The client engaged Tetra Engineering to analyze the problem and simulate the existing stresses during various load conditions. The scope of work included a review of historical failures and metallurgical reports, operational data analysis, Finite Element Analysis (FEA) and Fatigue Analysis.

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.

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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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