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Lubricant Deposit Characterization

Greg Livingstone
Exec. VP Bus Development
©2013. Fluitec. All Rights Reserved.
Deposit Issues
Deposits cause a host of problems
Sticking valves
Plugged lubricant orifices
Plugging filters
Inefficient heat exchanger operation
Bearing Lubrication
Loss of Seals

Page 2. ©2013 Fluitec. All Rights Reserved.
Why do we want to Characterize
Deposits?
1. To establish a condition monitoring program

2. To discover the root cause of fluid failure
3. To take proactive actions to improve the life
and performance of your lubricants.

Page 3. ©2013 Fluitec. All Rights Reserved.
How do We Analyze the Deposits

Page 4. ©2013 Fluitec. All Rights Reserved.
How do We Analyze the Deposits

Page 5. ©2013 Fluitec. All Rights Reserved.
Current Practices
Assume that all deposits or varnishes are
created equal.
Using visual characterization of a deposit
• assumes that since it is brown
• it must be the same as previously observed.

This assumption can be far from correct
Can lead to the wrong corrective actions.
Page 6. ©2013 Fluitec. All Rights Reserved.
Degradation & Deposit Formation
Oxidation

Thermal
Degradation

Contaminants

Other

Water

Additive
Drop-Out

Metal
Catalysts

MicroDieseling

Solids

Additive
Reaction Byproducts

Ultraviolet

Hot Spots

Gas

Formulation
Quality

Combustion

Incompatible
liquid

Incompatible
fluids

Air

Spark
Discharge

Page 7. ©2013 Fluitec. All Rights Reserved.
Analyzing the
Deposit

Page 8. ©2013 Fluitec. All Rights Reserved.
Characterizing
the Deposit

Page 9. ©2013 Fluitec. All Rights Reserved.
Common to have
multiple types of
deposits in a
system.

Page 10. ©2013 Fluitec. All Rights Reserved.
Classifying the Deposits
Deposits are classified by:
• Physical characteristics
• Source of formation
Based on this information, proactive measures
can be taken to eliminate deposit formation.

Page 11. ©2013 Fluitec. All Rights Reserved.
Beyond Academic – Case Studies

©2013 Fluitec. All rights reserved
Case Studies
1.
2.
3.
4.

Gas Turbine Tar Balls
Deposits in a Nuclear Power Plant
EHC system deposits
Dirty Gas Turbine Reservoir

Page 13. ©2013 Fluitec. All Rights Reserved.
1. Gas Turbine Tar Balls
A Large Frame Gas Turbine had an oil sample
that caused concern:

Page 14. ©2013 Fluitec. All Rights Reserved.
Significant deposits occurred during
the outage

When the fluid temperature got below 32oC large black tar-balls were observed
floating on the lube-oil surface in the tank and clogged hydraulic filters.
Page 15. ©2013 Fluitec. All Rights Reserved.
An Oil Reclamation Company helped
clean up the system

Page 16. ©2013 Fluitec. All Rights Reserved.
The Deposits were analyzed

3391

1027
3048

1156

2854

%T

693
1459
1303
2924

766
748

Varnish Isolated Fraction 1
1385

PHENYL-A-NAPHTHYL AMINE(PANA)

4000.0

•
•
•

3600

3200

2800

2400

2000

1800
cm-1

1589

1600

1400

1200

1000

800

605.0

Decomposed amine antioxidant derived from the lubricant
formulation.
The analysis identified this material as a mixture of unreacted and
reacted PANA.
The unreacted N-H from the PANA can easily be seen in FTIR at
3391 cm-1 along with the characteristic fingerprint stretches in the
1500-700 cm-1 region.
Page 17. ©2013 Fluitec. All Rights Reserved.
Isolated components identified foam
inhibitor
107.6
100
90
3452

80
70
60

1648
696

50

766

%T
864

40
2968
2859

30

2925

20

732

1455

Varnish Isolated Fraction 2
Acrylate Defoamant

937
1239
1372

10

1100 1020

1735

2.7
4000.0

3600

3200

2800

2400

2000

1800

1600

1400

1200

1000

800

600

450.0

cm-1

•
•

Acrylate polymer additive typically used to control foam
This additive could not be observed in the in-service fluids
from this system – nor could it be observed in the new fluid.
Page 18. ©2013 Fluitec. All Rights Reserved.
Composition of the Deposits
Source:
• Formulation
derived (Amine
Antioxidant)
• Contaminant
derived (Foam
Inhibitor)
Incompatible fluid
mixed into this
system.
Page 19. ©2013 Fluitec. All Rights Reserved.
Gas Turbine Plant Conclusions
Deployed a quality control program to ensure
incompatible lubricants do not accidentally get
added to the system.

Page 20. ©2013 Fluitec. All Rights Reserved.
2 – Deposits in a nuclear power plant
Sticking valve in a feed water pump caused an
expensive, 30-hour unplanned outage.
700-gallon reservoir using ISO
32 turbine oil.
Oil analysis results did not
reveal any problems.
•

MPC value was 16.

Deposits were gathered and
analyzed to determine their
source.

Page 21. ©2013 Fluitec. All Rights Reserved.
●

Investigation

1. Removed & analyzed
deposits from valve surface

2. Concentrated and analyzed
degradation products from the oil

Ref: Livingstone, Wooton
Page 22. ©2013 Fluitec. All Rights Reserved.
●

Deposit chemistry matched oil
chemistry
110

105

100

95

2924.37cm
-1

90
%T

1401.72cm
-1
1702.53cm - 1

85

838.35cm - 1

U2R16
MPC 42697

80

1116.31cm - 1

75
71
4000

3500

3000

2500

2000

1500

1000

650

cm -1
Ref: Livingstone, Wooton
Page 23. ©2013 Fluitec. All Rights Reserved.
●

Unique FTIR fingerprint was identified
Carboxylic acids were present as well as primary
amides.

Doublet indicate primary amides

Ref: Livingstone, Wooton
Page 24. ©2013 Fluitec. All Rights Reserved.
Source:
Oxidation and
contamination
from steam
leaks

Page 25. ©2013 Fluitec. All Rights Reserved.
●

Nuclear Power Plant Conclusions
Ammonia was present in the plant’s steam
chemistry.
Carboxylic Acids

Ammonia

Deposits
consisting of
Primary Amides

1. It was not feasible to remove sources of ammonia from
entering the system, but it is possible to remove acids.
2. In addition to MPC, plant is monitoring these units with
FTIR to measure acidic content and primary amide
production.
Ref: Livingstone, Wooton
Page 26. ©2013 Fluitec. All Rights Reserved.
3. EHC System Deposits
Rapid filter plugging and fluid failure was
experienced at a steam turbine plant causing an
outage.

Page 27. ©2013 Fluitec. All Rights Reserved.
Deposits were separated and analyzed
It is common for some
EHC systems to
experience microdieseling.
This creates dark oil and
black deposits.
Strong evidence of
thermal degradation.
Page 28. ©2013 Fluitec. All Rights Reserved.
Fluid & Deposits were analyzed

Page 29. ©2013 Fluitec. All Rights Reserved.
What type of thermal degradation?
ESD
Type of Deposit

Micro-Dieseling

High
Temperature

Thermoplastic

<1.0 micron soot- >1.0 micron
like particles
black particles

Black deposits indicated EHC
deposits caused by microdieseling or high temp
degradation.
Page 30. ©2013 Fluitec. All Rights Reserved.
Thermal Degradation
Paper Chromatography
was done to assist in
identifying particle size.
Very small particles will
go through the filter
unless varnish is present
to prevent it.
Analysis indicated it was
not from micro-dieseling.
Page 31. ©2013 Fluitec. All Rights Reserved.
Thermal Degradation
Microscopic
evaluation revealed
particles >5microns in size.

Page 32. ©2013 Fluitec. All Rights Reserved.
EHC Deposit Conclusions
Instead of fixing the assumed micro-dieseling
problem, the plant focused on potential sources of
high heat.
Malfunctioning pump was found to produce
temperatures of 500oF.

Repaired the pump, solving rapid fluid
degradation.

Page 33. ©2013 Fluitec. All Rights Reserved.
4. Dirty Gas Turbine Reservoir

Very dark and wide bathtub ring, reservoir deposits and varnish through the inside of
a 7FA gas turbine.

Page 34. ©2013 Fluitec. All Rights Reserved.
●

Impossible to Wipe off!
@#$&!!!

Ref: Livingstone,
Page 35. ©2013 Fluitec. All Rights Reserved.
●

Deposits derived from Polyacrylate
Foam Inhibitor
99.6

90

80

70

60

%T

50

40

30

20

10
2.8
4000.0

3600

3200

2800

2400

2000

1800

1600

1400

1200

1000

800

600

450.0

cm-1

System Deposit
POLYACRYLATE DEFOMANT
Ref: Livingstone, Wooton
Page 36. ©2013 Fluitec. All Rights Reserved.
Conclusions
1. There are many possible modes of fluid
degradation.
2. Your condition monitoring program should be
based on the failure mode of the fluid.
3. Understanding the mode of failure allows you
to address the root cause.
4. Most importantly, don’t make assumptions!
Let the data drive the decisions.

Page 37. ©2013 Fluitec. All Rights Reserved.
Acknowledgements
1. Dr. Dave Wooton was involved in these root
cause analysis and has co-authored
multiple papers with me on this subject.
2. TestOil provided laboratory support to these
projects and has developed leading deposit
characterization services.

Page 38. ©2013 Fluitec. All Rights Reserved.

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Lubricant Deposit Characterization, Greg Livingstone, Fluitec

  • 1. Lubricant Deposit Characterization Greg Livingstone Exec. VP Bus Development ©2013. Fluitec. All Rights Reserved.
  • 2. Deposit Issues Deposits cause a host of problems Sticking valves Plugged lubricant orifices Plugging filters Inefficient heat exchanger operation Bearing Lubrication Loss of Seals Page 2. ©2013 Fluitec. All Rights Reserved.
  • 3. Why do we want to Characterize Deposits? 1. To establish a condition monitoring program 2. To discover the root cause of fluid failure 3. To take proactive actions to improve the life and performance of your lubricants. Page 3. ©2013 Fluitec. All Rights Reserved.
  • 4. How do We Analyze the Deposits Page 4. ©2013 Fluitec. All Rights Reserved.
  • 5. How do We Analyze the Deposits Page 5. ©2013 Fluitec. All Rights Reserved.
  • 6. Current Practices Assume that all deposits or varnishes are created equal. Using visual characterization of a deposit • assumes that since it is brown • it must be the same as previously observed. This assumption can be far from correct Can lead to the wrong corrective actions. Page 6. ©2013 Fluitec. All Rights Reserved.
  • 7. Degradation & Deposit Formation Oxidation Thermal Degradation Contaminants Other Water Additive Drop-Out Metal Catalysts MicroDieseling Solids Additive Reaction Byproducts Ultraviolet Hot Spots Gas Formulation Quality Combustion Incompatible liquid Incompatible fluids Air Spark Discharge Page 7. ©2013 Fluitec. All Rights Reserved.
  • 8. Analyzing the Deposit Page 8. ©2013 Fluitec. All Rights Reserved.
  • 9. Characterizing the Deposit Page 9. ©2013 Fluitec. All Rights Reserved.
  • 10. Common to have multiple types of deposits in a system. Page 10. ©2013 Fluitec. All Rights Reserved.
  • 11. Classifying the Deposits Deposits are classified by: • Physical characteristics • Source of formation Based on this information, proactive measures can be taken to eliminate deposit formation. Page 11. ©2013 Fluitec. All Rights Reserved.
  • 12. Beyond Academic – Case Studies ©2013 Fluitec. All rights reserved
  • 13. Case Studies 1. 2. 3. 4. Gas Turbine Tar Balls Deposits in a Nuclear Power Plant EHC system deposits Dirty Gas Turbine Reservoir Page 13. ©2013 Fluitec. All Rights Reserved.
  • 14. 1. Gas Turbine Tar Balls A Large Frame Gas Turbine had an oil sample that caused concern: Page 14. ©2013 Fluitec. All Rights Reserved.
  • 15. Significant deposits occurred during the outage When the fluid temperature got below 32oC large black tar-balls were observed floating on the lube-oil surface in the tank and clogged hydraulic filters. Page 15. ©2013 Fluitec. All Rights Reserved.
  • 16. An Oil Reclamation Company helped clean up the system Page 16. ©2013 Fluitec. All Rights Reserved.
  • 17. The Deposits were analyzed 3391 1027 3048 1156 2854 %T 693 1459 1303 2924 766 748 Varnish Isolated Fraction 1 1385 PHENYL-A-NAPHTHYL AMINE(PANA) 4000.0 • • • 3600 3200 2800 2400 2000 1800 cm-1 1589 1600 1400 1200 1000 800 605.0 Decomposed amine antioxidant derived from the lubricant formulation. The analysis identified this material as a mixture of unreacted and reacted PANA. The unreacted N-H from the PANA can easily be seen in FTIR at 3391 cm-1 along with the characteristic fingerprint stretches in the 1500-700 cm-1 region. Page 17. ©2013 Fluitec. All Rights Reserved.
  • 18. Isolated components identified foam inhibitor 107.6 100 90 3452 80 70 60 1648 696 50 766 %T 864 40 2968 2859 30 2925 20 732 1455 Varnish Isolated Fraction 2 Acrylate Defoamant 937 1239 1372 10 1100 1020 1735 2.7 4000.0 3600 3200 2800 2400 2000 1800 1600 1400 1200 1000 800 600 450.0 cm-1 • • Acrylate polymer additive typically used to control foam This additive could not be observed in the in-service fluids from this system – nor could it be observed in the new fluid. Page 18. ©2013 Fluitec. All Rights Reserved.
  • 19. Composition of the Deposits Source: • Formulation derived (Amine Antioxidant) • Contaminant derived (Foam Inhibitor) Incompatible fluid mixed into this system. Page 19. ©2013 Fluitec. All Rights Reserved.
  • 20. Gas Turbine Plant Conclusions Deployed a quality control program to ensure incompatible lubricants do not accidentally get added to the system. Page 20. ©2013 Fluitec. All Rights Reserved.
  • 21. 2 – Deposits in a nuclear power plant Sticking valve in a feed water pump caused an expensive, 30-hour unplanned outage. 700-gallon reservoir using ISO 32 turbine oil. Oil analysis results did not reveal any problems. • MPC value was 16. Deposits were gathered and analyzed to determine their source. Page 21. ©2013 Fluitec. All Rights Reserved.
  • 22. ● Investigation 1. Removed & analyzed deposits from valve surface 2. Concentrated and analyzed degradation products from the oil Ref: Livingstone, Wooton Page 22. ©2013 Fluitec. All Rights Reserved.
  • 23. ● Deposit chemistry matched oil chemistry 110 105 100 95 2924.37cm -1 90 %T 1401.72cm -1 1702.53cm - 1 85 838.35cm - 1 U2R16 MPC 42697 80 1116.31cm - 1 75 71 4000 3500 3000 2500 2000 1500 1000 650 cm -1 Ref: Livingstone, Wooton Page 23. ©2013 Fluitec. All Rights Reserved.
  • 24. ● Unique FTIR fingerprint was identified Carboxylic acids were present as well as primary amides. Doublet indicate primary amides Ref: Livingstone, Wooton Page 24. ©2013 Fluitec. All Rights Reserved.
  • 25. Source: Oxidation and contamination from steam leaks Page 25. ©2013 Fluitec. All Rights Reserved.
  • 26. ● Nuclear Power Plant Conclusions Ammonia was present in the plant’s steam chemistry. Carboxylic Acids Ammonia Deposits consisting of Primary Amides 1. It was not feasible to remove sources of ammonia from entering the system, but it is possible to remove acids. 2. In addition to MPC, plant is monitoring these units with FTIR to measure acidic content and primary amide production. Ref: Livingstone, Wooton Page 26. ©2013 Fluitec. All Rights Reserved.
  • 27. 3. EHC System Deposits Rapid filter plugging and fluid failure was experienced at a steam turbine plant causing an outage. Page 27. ©2013 Fluitec. All Rights Reserved.
  • 28. Deposits were separated and analyzed It is common for some EHC systems to experience microdieseling. This creates dark oil and black deposits. Strong evidence of thermal degradation. Page 28. ©2013 Fluitec. All Rights Reserved.
  • 29. Fluid & Deposits were analyzed Page 29. ©2013 Fluitec. All Rights Reserved.
  • 30. What type of thermal degradation? ESD Type of Deposit Micro-Dieseling High Temperature Thermoplastic <1.0 micron soot- >1.0 micron like particles black particles Black deposits indicated EHC deposits caused by microdieseling or high temp degradation. Page 30. ©2013 Fluitec. All Rights Reserved.
  • 31. Thermal Degradation Paper Chromatography was done to assist in identifying particle size. Very small particles will go through the filter unless varnish is present to prevent it. Analysis indicated it was not from micro-dieseling. Page 31. ©2013 Fluitec. All Rights Reserved.
  • 32. Thermal Degradation Microscopic evaluation revealed particles >5microns in size. Page 32. ©2013 Fluitec. All Rights Reserved.
  • 33. EHC Deposit Conclusions Instead of fixing the assumed micro-dieseling problem, the plant focused on potential sources of high heat. Malfunctioning pump was found to produce temperatures of 500oF. Repaired the pump, solving rapid fluid degradation. Page 33. ©2013 Fluitec. All Rights Reserved.
  • 34. 4. Dirty Gas Turbine Reservoir Very dark and wide bathtub ring, reservoir deposits and varnish through the inside of a 7FA gas turbine. Page 34. ©2013 Fluitec. All Rights Reserved.
  • 35. ● Impossible to Wipe off! @#$&!!! Ref: Livingstone, Page 35. ©2013 Fluitec. All Rights Reserved.
  • 36. ● Deposits derived from Polyacrylate Foam Inhibitor 99.6 90 80 70 60 %T 50 40 30 20 10 2.8 4000.0 3600 3200 2800 2400 2000 1800 1600 1400 1200 1000 800 600 450.0 cm-1 System Deposit POLYACRYLATE DEFOMANT Ref: Livingstone, Wooton Page 36. ©2013 Fluitec. All Rights Reserved.
  • 37. Conclusions 1. There are many possible modes of fluid degradation. 2. Your condition monitoring program should be based on the failure mode of the fluid. 3. Understanding the mode of failure allows you to address the root cause. 4. Most importantly, don’t make assumptions! Let the data drive the decisions. Page 37. ©2013 Fluitec. All Rights Reserved.
  • 38. Acknowledgements 1. Dr. Dave Wooton was involved in these root cause analysis and has co-authored multiple papers with me on this subject. 2. TestOil provided laboratory support to these projects and has developed leading deposit characterization services. Page 38. ©2013 Fluitec. All Rights Reserved.