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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Papers, Presentations and Articles

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

Title
Author
Combined Cycle Plants - O&M problems not caused by cycling
Combined Cycle Plants - O&M problems not caused by cyclingCombined Cycle Plants - O&M problems not caused by cycling
P.S. Jackson, D.S. Moelling, J.W. Malloy (Tetra)
May 15, 2007, Power Magazine
First-class maintenance in a developing country
First-class maintenance in a developing countryFirst-class maintenance in a developing country
F.J. Berté, (Tetra ); J. Sandoval, (Tekna S.A.); A. Carrillo (Gensa S.A)
Feb 15, 2007, Power Magazine
O&M staff keep their cool at Alaskan plant
O&M staff keep their cool at Alaskan plantO&M staff keep their cool at Alaskan plant
P.S. Jackson (Tetra ) and John Kotrotsios (Chugach Electric Association)
Mar 15, 2006, Power Magazine
Operating Experience of Large Reheat HRSGs in Merchant Service
Operating Experience of Large Reheat HRSGs in Merchant ServiceOperating Experience of Large Reheat HRSGs in Merchant Service
P.S. Jackson, D.S. Moelling, F.C. Anderson, J.W. Malloy (Tetra)
2004, POWERGEN INT., USA,
HRSG Tube Failures: Prediction, Diagnosis and Corrective Actions
HRSG Tube Failures: Prediction, Diagnosis and Corrective ActionsHRSG Tube Failures: Prediction, Diagnosis and Corrective Actions
F.C. Anderson, P.S. Jackson, D.S. Moelling (Tetra) and F. Glasgow (PGE NEG - Hermiston)
Mar 2003, NACE Corrosion/2003 Expo, San Diego

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 GRP Piping Caustic Dosing, 2018
Middle East.

CFD Analysis of GRP Piping Caustic Dosing, 2018

Caustic soda is injected into the product water in order to raise the pH as required by the specification. Inspection of GRP piping has often shown large amounts of deposition inside these pipes. Deposition is mostly observed downstream of the injection point of sodium hydroxide and can therefore be attributed to unsuitable chemical injection. Typical injection setups utilise four simple (no nozzle) injection ports at 90° from one another causing ineffective mixing of the flows, leading to the observed precipitation. Tetra performed a CFD analysis of the caustic injection process to investigate the degree of mixing of the two flows and simulate the effects of modifying the volumetric flow rate.

MSV Stellite Cracking Failure Analysis, 2018
Middle East.

MSV Stellite Cracking Failure Analysis, 2018

Caustic soda is injected into the product water in order to raise the pH as required by the specification. Inspection of GRP piping has often shown large amounts of deposition inside these pipes. Deposition is mostly observed downstream of the injection point of sodium hydroxide and can therefore be attributed to unsuitable chemical injection. Typical injection setups utilise four simple (no nozzle) injection ports aStaff at a CCGT plant engaged Tetra to investigate the root cause of the cracking and damage appearing on the Main Steam Valve (MSV) stellite seat ring(s). The metallurgical analysis identified iron dilution from the F91 valve seat into the hard-facing alloy as the root cause of the debonding.  The extent of the iron dilution is a sign of excessive heat input, most likely caused during the welding process. This points towards the welding during fabrication as the actual root cause of the failure. The driving force for failure / debonding of the Stellite hardfacing could also include residual stresses from welding and/or transient heat transfer stresses and/or thermal shock during operation.t 90° from one another causing ineffective mixing of the flows, leading to the observed precipitation. Tetra performed a CFD analysis of the caustic injection process to investigate the degree of mixing of the two flows and simulate the effects of modifying the volumetric flow rate.

Root Cause Analysis of HP Drum Nozzle Cracking, 2018
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.

Diverter Damper Design & Operation Review, 2018
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

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