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1 HRSG Inspection Tasks Presented By: Bryan F. Craig, P.E HRST Inc. AEP / BRO Forum 8/10/2009 Columbus, OH 1 HRSG Inspection Goals: 1. Document condition of equipment 2. Identify items that need immediate maintenance 3. Identify items that need budgeting and planning for maintenance next year 4. Identifyproblems early, allowing time for scrutiny and analysis 5. Due diligence…..show stakeholders you have proactive approach. AEP / BRO Forum 8/10/2009 Columbus, OH 2

HRSG Inspection Basic Tasks

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HRSG Inspection Tasks

Presented By:Bryan F. Craig, P.EHRST Inc.

AEP / BRO Forum8/10/2009 Columbus, OH 1

HRSG Inspection

Goals:

1. Document condition of equipment

2. Identify items that need immediate maintenance

3. Identify items that need budgeting and planning for maintenance next year

4. Identify problems early, allowing time for  y p y, gscrutiny and analysis

5. Due diligence…..show stakeholders you have proactive approach.

AEP / BRO Forum8/10/2009 Columbus, OH 2

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HRSG Inspection

Key Elements

1. Dedicated inspectors• Good inspections take days not hours!• Good inspections take days not hours!

2. Recording observations (facts)• Photos, measurements, notes

3. Organize facts logically• Every fact should be accurately linked to a specific location.

4. Measurements at critical areas• Thickness (UT), Gap distance, crack length

5. Three location types• Gas Path

• Steam/Water Side

• ExteriorAEP / BRO Forum8/10/2009 Columbus, OH 3

HRSG InspectionGas‐Side Inspection Areas

• Access Lanes (inlet duct, firing duct, SCR, l b t t b b dl t k)lanes between tube bundles, stack)

• Crawl spaces under and above tube headers

• Important to document locations clearly for future referencefuture reference

• Best to prepare in advance, rather than identify problem locations “on the fly”

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Gas‐Side Tasks

Inlet Duct Items:*

1 Liner System1. Liner System

– Loose plates, spinning washers, exposed insulation, failed studs.

2. Flow distribution plates or vanes

3. Tubes & Fins

corrosion warping vibration wear– corrosion, warping, vibration wear

4. Baffles & Tube Ties

– vibration damage, wear, expansion interferences, weld cracks.

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Inlet Duct LinerLoose & broken components

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Inlet Duct LinerSpinning Washers

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Inlet Duct LinerLiner Gaps, Exposed Insulation

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Flow Distribution Grid

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Tube Ties

Tube & fin wearTube & fin wear at tube tie

AEP / BRO Forum8/10/2009 Columbus, OH 11

Failed Tube Ties

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Gas‐Side Tasks

Firing Duct Checklist1. Liner System (same as inlet duct, plus look for oxidized 

components)p )2. Duct Burner:

– Sag in elements or baffles– Nozzle plugging– Coke buildup– Burner “wing” condition

3. Tubes & Fins (same as inlet duct, plus)– Evidence of flame impingement or local hotspotsEvidence of flame impingement or local hotspots

4. Baffles & Supports5. Location of firing duct thermocouples

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Reheater upstream of duct burner

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Burner Baffle Failures

Coen baffle weld seam cracks & failures

Coen fix for baffle weld seam cracks & failures.

May not be enough, some cracking still being found.

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Carbon Buildup

Carbon inside gas pipe. Build up has fractured the

Coking: Usually due to olefins in refinery gas. Sometimes coking occurs with natural gas due to poor air/fuel mixing at burner.

gas pipe.

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Oxidized Liner Components

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Local Burner Hotspots

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Gas‐Side Tasks

Tube Bundle Access Lane Checklist:1. Liner System (same checks as inlet & firing y ( g

ducts, problems less prevalent)2. Tubes & Fins: corrosion, warping3. Baffles & Supports (same as previous)4. Catalyst

– Foulingg– Gas bypass around perimeter– Packing between blocks

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Tube & Fin Fouling

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Tubes & FinsTube Buckling – Superheaters & Economizers

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Tubes & FinsCracking – HPSH Tube

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Gas Baffles Exhaust flow into page

Sidewall Baffles

Tubes

Upper Header

Sidewall Baffles

Center (Laning) Baffles

Lower Header

Header (Bulkhead)

Baffles

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Baffle Failures

AEP / BRO Forum8/10/2009 Columbus, OH 25

Baffle Gaps Decrease Performance

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Catalyst Fouling

Catalyst Gas Bypass

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Gas‐Side Tasks

Crawl Space Checklist:1. Water from tube leaks?2. Floor debris3. Liner condition4. Liner fit‐up around piping and hanger 

penetrations5. Baffles6 Bent piping6. Bent piping7. Header corrosion8. Tube/header joint condition (if visible)

AEP / BRO Forum8/10/2009 Columbus, OH 29

Spray pattern is a leak indication

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Fin scale debris on crawlspace floor

Oxidized carbon steel debris on crawlspace floor

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Roof debris blocks drainage holes, trapping rainwater.

Accelerated corrosion near penetrations, probably caused by rain water leaking past penetration seal.

AEP / BRO Forum8/10/2009 Columbus, OH 34

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Bulkhead Gas Bypass

HotExh

AEP / BRO Forum8/10/2009 Columbus, OH 35

Gap between baffle and floor is too large, allows

gas bypass, decreasing

performance.

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Bent Drains Indicate Stress

AEP / BRO Forum8/10/2009 Columbus, OH 37

Exterior Tasks

Exterior Inspection ChecklistExterior Inspection Checklist

1. Casing hotspots, cracks

2. Piping penetration seals

3. Access door condition

4 Foundations4. Foundations

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CasingAccess Doors – Hot Spot

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Penetration Seals

Bellows cracks can be difficult to see. Tight cracks, bellows are

compressed when off line. Look for hot spots, and nearby insulation

“fur.”

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These bellow cracks were easy to see!

However, it took some extra effort to climb up on the roof casing to

inspect.

AEP / BRO Forum8/10/2009 Columbus, OH 41

PROBLEM:

T i F b i

HRST Upgraded Pipe Penetration Seal

Tears in Fabric

Cracks in Bellows

SOLUTION:

Delay box

SOLUTION:

HRST Pipe Penetration Seals

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Casing Stress & Cracks

Expansion

Stress Points (Typ)

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Casing Stress & Cracks

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Casing Crack

Hotspots

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HRSG InspectionWater/Steam‐Side Tasks

Steam Drums are the only non‐intrusive access yto the water/steam side in a modern HRSG.

Drums are often also inspected by the water chemistry dept and insurance inspector.

AEP / BRO Forum8/10/2009 Columbus, OH 47

Water/Steam‐Side Inspection Tasks

Steam Drum Checklist1. Drum surface condition2. Signs of distress on steam separation 

equipment & belly pan3. Thickness of belly plates and steam 

separators4. Mechanical Integrityg y5. Approximate waterline vs. drawing6. Debris

AEP / BRO Forum8/10/2009 Columbus, OH 48

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Drum Surface Condition

1. Drum surface details (color, condition, pits)

– Color– Red is good in an oxidizing environment

– Red is bad in a reducing environment

– Condition– Keep track of surface defects from manufacture

– Track whether smoothness (roughness) is changing

– PitsPits – Do you have them?  

– What do they look like underneath?

AEP / BRO Forum8/10/2009 Columbus, OH 49

Oxygen Attack in Steam Drum ‐Offline

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HP Drum Condition

Surface defects in an HP drum from rolling steel NOT a significant issue

AEP / BRO Forum8/10/2009 Columbus, OH 51

Signs of Distress

2. Signs of distress on steam separation equipment & belly panequipment & belly pan

– Cracks in the belly pan

– Cracks in the final separator corners

– Weld seams in the shell and shell to head

– Downcomer indications

AEP / BRO Forum8/10/2009 Columbus, OH 52

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Cracks?

Signs of Distress

Baffle Cracks?

AEP / BRO Forum8/10/2009 Columbus, OH 53

HP – Belly Pan Cracks (or baffle plate)

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Downcomer Indications

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Thickness of Belly Pans and Steam Separation Equipment

33. UT test

– F/W, Deltak, Vogt, NEM, Aalborg, Alstom, etc– Belly Pans

– Cyclones (F/W = horizontal, others = vertical)

– N/E and Cerrey– Belly Pans (no cyclones)

AEP / BRO Forum8/10/2009 Columbus, OH 56

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Ultrasonic Thickness Measurements

– Thickness measurements are a useful tool to document condition of drum internals, tubes and ,piping.

– Be specific about locations & documentation

– Most measurements are simple thickness for general documentation or to track Flow Accelerated Corrosion

h d d f k d– More sophisticated UT used for crack detection:  shear wave, phased array

AEP / BRO Forum8/10/2009 Columbus, OH 57

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Cyclones worn through from FAC

AEP / BRO Forum8/10/2009 Columbus, OH 59

Belly Pan Thinning –UT in LP & IP

Check here!

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LP Belly Pan Hole (FAC)

AEP / BRO Forum8/10/2009 Columbus, OH 61

Mechanical Integrity

i f l4. Integrity of Internals

– Piping– Broken ‘U’ Bolts

– Missing nuts

– Plugged Chem Feed Lines

– Separators– Failure

– Plugging

– Missing hardware

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HP – Fallen Chem Feed Line

U bolt broke off

AEP / BRO Forum8/10/2009 Columbus, OH 63

HP Drum – Chem Feed Line

AEP / BRO Forum8/10/2009 Columbus, OH 64

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HP Drum – broken cyclone attachment

AEP / BRO Forum8/10/2009 Columbus, OH 65

Deltak – Perforated Plate Above Mesh Separator

AEP / BRO Forum8/10/2009 Columbus, OH 66

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Deltak ‐Mesh Separator Failure

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Approximate Water Line vs. Drawing

i di5. Water Line Readings

– The water line is often falsely reading low due to –proximity of the downcomer or pump suction to the level transmitters.  The suction effect of those large lines ‘pulls’ on the level sensing lines. 

– Plugging of the lines is problematic if they are positioned off the bottom of the shell.  

– The number one cause of faulty level indication or control is calibration or compensation

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LP – water level

AEP / BRO Forum8/10/2009 Columbus, OH 69

LP – level transmitter proximity to pump suction

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Debris in level tap

Lower level tap magnetic debris

AEP / BRO Forum8/10/2009 Columbus, OH 71

Debris in Drums

6 b i6. Debris

– Amount

– Color

– Magnetite vs. Hematite?

– Flakes vs. Powder?

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Debris in drum

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• Gas Side – Access Lanes (inlet duct, firing duct, SCR, between tube

Summary

Access Lanes (inlet duct, firing duct, SCR, between tube bundles, stack)

– Crawl spaces under and above tube headers

• Exterior– Casing hotspots, cracks– Piping penetration seals– Access door condition– Foundations– Foundations

• Steam/Water Side– Steam Drums are the only non‐intrusive access to the 

water/steam side in most HRSGs

AEP / BRO Forum8/10/2009 Columbus, OH 74

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HRSG InspectionFurther Work

• Online or “Hot” Inspection– HRSG inspection while unit is operating– Ideal for finding hotspots, casing cracks, penetration seal failuresg p , g , p– Can check hot position of spring hangers

• “Extended Scope” offline inspection– Depending on the age, quantity & severity of cycles and history of issues, 

more intrusive inspection techniques may be best to quantify condition.– Common techniques:

1. UT tubes and piping beyond spot checks (A Scan, Phased Array, or Shear Wave)2. Dye Penetrant or Magnetic particle testing of suspect areas3. Conventional and Digital X‐Ray (Radiography)4. Eddy Current Testing5. Piping Assessment6. Hardness and Replication (P91)7. Desuperheater removal & inspection8. Borescoping9. Tube samples

AEP / BRO Forum8/10/2009 Columbus, OH 75

Any Questions?

Bryan F. Craig, P.EHRST [email protected]‐855‐4688 (office)612‐743‐1009 (cell

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