HRSG Inspection Tasks

April 5, 2018 | Author: mkarahan | Category: Duct (Flow), Basement, Vacuum Tube, Corrosion, Pump
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Inspection Guide for HRSG...

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HRSG Inspection Tasks

Presented By: Bryan F. Craig, P.E HRST Inc.

8/10/2009 Columbus, OH

AEP / BRO Forum

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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 yp y, g 4. Identify problems early, allowing time for   scrutiny and analysis 5. Due diligence…..show stakeholders you have  proactive approach. 8/10/2009 Columbus, OH

AEP / BRO Forum

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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 Exterior

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HRSG Inspection Gas‐Side Inspection Areas

• Access Lanes (inlet duct, firing duct, SCR,  l lanes between tube bundles, stack) b t t b b dl t k) • Crawl spaces under and above tube  headers • Important to document locations clearly for  future reference future reference • Best to prepare in advance, rather than  identify problem locations “on the fly” 8/10/2009 Columbus, OH

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Gas‐Side Tasks Inlet Duct Items:* 1 Liner System 1. 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 Liner Loose & broken components

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Inlet Duct Liner Spinning Washers

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Inlet Duct Liner Liner Gaps, Exposed Insulation

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Flow Distribution Grid

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Tube Ties

Tube & fin wear at tube tie

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Failed Tube Ties

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Gas‐Side Tasks Firing Duct Checklist 1. Liner System (same as inlet duct, plus look for oxidized  components) p ) 2. Duct Burner: – – – –

3.

Tubes & Fins (same as inlet duct, plus) –

4. 5.

Sag in elements or baffles Nozzle plugging Coke buildup Burner “wing” condition Evidence of flame impingement or local hotspots Evidence of flame impingement or local hotspots

Baffles & Supports Location of firing duct thermocouples

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Reheater upstream of duct burner 8/10/2009 Columbus, OH

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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. 8/10/2009 Columbus, OH

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Carbon Buildup

Carbon inside gas pipe. Build up has fractured the gas pipe.

Coking: Usually due to olefins in refinery gas. Sometimes coking occurs with natural gas due to poor air/fuel mixing at burner. 8/10/2009 Columbus, OH

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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, warping 3. Baffles & Supports (same as previous) 4. Catalyst – Foulingg – Gas bypass around perimeter – Packing between blocks

8/10/2009 Columbus, OH

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Tube & Fin Fouling

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Tubes & Fins Tube Buckling – Superheaters & Economizers

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Tubes & Fins Cracking – HPSH Tube

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Gas Baffles 

Exhaust flow into page

Sidewall Baffles Upper Header Center (Laning) Baffles

Tubes

Lower Header Header (Bulkhead) Baffles

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Baffle Failures

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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 debris 3. Liner condition 4. Liner fit‐up around piping and hanger  penetrations 5. Baffles 6 Bent piping 6. Bent piping 7. Header corrosion 8. Tube/header joint condition (if visible)

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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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Accelerated corrosion near penetrations, probably caused by rain water leaking past penetration seal. 8/10/2009 Columbus, OH

Roof debris blocks drainage holes, trapping rainwater.

AEP / BRO Forum

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Bulkhead Gas Bypass

Hot Exh

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Gap between baffle and floor is too large, allows gas bypass, decreasing performance.

8/10/2009 Columbus, OH

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Bent Drains Indicate Stress

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Exterior Tasks Exterior Inspection Checklist Exterior Inspection Checklist 1. Casing hotspots, cracks 2. Piping penetration seals 3. Access door condition 4 Foundations 4.

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Casing Access 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.” 8/10/2009 Columbus, OH

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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. 8/10/2009 Columbus, OH

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HRST Upgraded Pipe Penetration Seal

PROBLEM: T Tears in i Fabric F bi Cracks in Bellows Delay box

SOLUTION: HRST Pipe Penetration Seals

8/10/2009 Columbus, OH

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Casing Stress & Cracks

Expansion

Stress Points (Typ) 8/10/2009 Columbus, OH

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Casing Stress & Cracks

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Casing Crack

Hotspots

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HRSG Inspection Water/Steam‐Side Tasks

Steam Drums are the only non‐intrusive access  y to the water/steam side in a modern HRSG. Drums are often also inspected by the water  chemistry dept and insurance inspector.

8/10/2009 Columbus, OH

AEP / BRO Forum

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Water/Steam‐Side Inspection Tasks Steam Drum Checklist 1. Drum surface condition 2. Signs of distress on steam separation  equipment & belly pan 3. Thickness of belly plates and steam  separators 4. Mechanical Integrity g y 5. Approximate waterline vs. drawing 6. Debris 8/10/2009 Columbus, OH

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Drum Surface Condition 1. Drum surface details (color, condition, pits) –

Color – –



Condition – –



Red is good in an oxidizing environment Red is bad in a reducing environment Keep track of surface defects from manufacture Track whether smoothness (roughness) is changing

Pits  Pits – –

Do you have them?   What do they look like underneath?

8/10/2009 Columbus, OH

AEP / BRO Forum

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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 8/10/2009 Columbus, OH AEP / BRO Forum

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

Cracks in the belly pan Cracks in the final separator corners Weld seams in the shell and shell to head Downcomer indications

8/10/2009 Columbus, OH

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Signs of Distress Cracks?

Baffle Cracks?

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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 3. 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)

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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 More sophisticated UT used for crack detection:   h d df kd shear wave, phased array

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Cyclones worn through  from FAC

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Belly Pan Thinning – UT in LP & IP Check here!

8/10/2009 Columbus, OH

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LP Belly Pan Hole (FAC)

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Mechanical Integrity 4. Integrity of Internals i f l –

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

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HP Drum – Chem Feed Line

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HP Drum – broken cyclone attachment

8/10/2009 Columbus, OH

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Deltak – Perforated Plate Above  Mesh Separator

8/10/2009 Columbus, OH

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Deltak ‐ Mesh Separator Failure

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Approximate Water Line  vs. Drawing 5. Water Line Readings i di – 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 8/10/2009 Columbus, OH

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LP – water level

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LP – level transmitter proximity  to pump suction

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Debris in level tap

Lower level tap magnetic debris 8/10/2009 Columbus, OH

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Debris in Drums 6 Debris 6. bi – – – –

Amount Color Magnetite vs. Hematite? Flakes vs. Powder?

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Debris in drum

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Summary •

Gas Side  – –



Exterior – – – –



Access Lanes (inlet duct, firing duct, SCR, between tube Access Lanes (inlet duct, firing duct, SCR, between tube  bundles, stack) Crawl spaces under and above tube headers Casing hotspots, cracks Piping penetration seals Access door condition Foundations

Steam/Water Side –

Steam Drums are the only non‐intrusive access to the  water/steam side in most HRSGs

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HRSG Inspection Further Work • Online or “Hot” Inspection – HRSG inspection while unit is operating – Ideal for finding hotspots, casing cracks, penetration seal failures g 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. 2. 3. 4. 5. 6. 7. 8. 9.

UT tubes and piping beyond spot checks (A Scan, Phased Array, or Shear Wave) Dye Penetrant or Magnetic particle testing of suspect areas Conventional and Digital X‐Ray (Radiography) Eddy Current Testing Piping Assessment Hardness and Replication (P91) Desuperheater removal & inspection Borescoping Tube samples

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Any Questions? Bryan F. Craig, P.E HRST Inc. [email protected] 813‐855‐4688 (office) 612‐743‐1009 (cell

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