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Evaluating the Long-Term Performance of
Composite Wear Rings in Centrifugal Pumps

Robert Aronen, Boulden International: Robert Aronen is the Managing
Director, EMEA, for Boulden International in Luxembourg. Since 2002, he has been
developing the market for the composite material DuPont™ Vespel® CR-6100 in
centrifugal pump applications. His prior work includes 4 years as a rotating equipment
engineer in the refining industry and 6 years as an engineer for Flowserve, Fluid Sealing
Division.
Mr. Aronen received a B.S. degree (Mechanical Engineering, 1991) from Rose-Hulman
Institute of Technology.

Martin Russek, Sunoco: Martin Russek is a Rotating Equipment Reliability Engineer at
the Sunoco, Philadelphia Refinery. He has worked in several rotating equipment
reliability roles for Sunoco at their 3 refineries in the Northeast since 1999. He has been
responsible for numerous pump, compressor, and turbine upgrades. Prior to his work in
the refineries, he was a Systems Engineer and Maintenance Engineer for Public Service
Electric & Gas Company. He has a Level II vibration certification and is an INPO certified
Systems Engineer.
Mr. Russek received a B.S. degree (Mechanical Engineering, 1989) from Trenton State
College.
Background
• Refinery instituted a reliability improvement
  program to install composite wear rings as a
  standard upgrade to all bad-actor pumps
• Initial results were published at 2007
  International Pump Users Symposium
• This Case Study provides long-term results
  after more than 4 years of running time
Program Scope
61 Centrifugal Pumps

Temperatures from 65 ⁰F (17 ⁰C) to 475 ⁰F (246 ⁰C)

Hydrocarbon, Acid, Amine, Water, Caustic services

Multiple API horizontal and vertical pump types

Intermittent (tank farm, product transfer) and
continuous process services
Which Components?

Horizontal Pumps        Vertical Pumps
Stationary wear rings   Stationary wear rings
Inter-stage rings       Bowl bearings
Center-stage bushings   Line-shaft bearings
Throttle bushings       Throat bushings
Throat bushings
Why Composite Wear Rings?
• No metal-to-metal contact
  – Avoid seizure
  – Survive process upsets
• Reduced Clearance
  –   Lomakin Effect
  –   Lower vibration
  –   Reduced shaft deflection
  –   Lower NPSHR
Material Selected: PFA/CF Composite
Key Properties
Coefficient of thermal expansion (x-y)*   3.1 X 10-6 (in/in/⁰F)     ASTM E-831
                                          5.6 X 10-6 (mm/mm/⁰C)
Temperature Limit*                        500 ⁰F (260 ⁰C)           ASTM D-648
Limiting PV*                              278000 (psi-ft/min)       Falex test
                                          9.7 (Mpa-m/sec)
Chemically compatible with everything in the refinery
Favorable machining and installation characteristics




                                                        *Source: DuPont™ Vespel® CR-6100
Definitions
Repair      Any work order—includes seals, bearings,
            vibration issues, wear ring seizure, inability to
            make rate, etc… with an associated cost
Overall     Average of 111 vibration data points from the
Vibration   25 horizontal pumps within the study
            population.
LDAR Seal   Leak Detection and Repair (LDAR) program,
Leaks       which monitors single mechanical seals in VOC
            (volatile organic compound) services.
Results from Original Study
                    2003—2006
          Factor Studied                     Change

          Number of Repairs                  45% Reduction

          Overall Vibration                  25% Reduction

          LDAR Seal Leaks                    70% Reduction


*Source: Aronen, R., Boulden, B., and Russek, M., 2007, “Driving Pump Reliability
Forward with Advanced Composite Wear Rings,” Proceedings of the 23rd
International Pump Users Symposium, Turbomachinery Laboratory, Texas A&M
University, College Station, Texas, pp. 15-19.
Long Term Results: 2000—2009
Annual Repairs
                                    (Population 61 Pumps)
                 60

                 50

                 40
Annual Repairs




                                                                          Composite Repairs
                 30
                                                                          Metal Repairs
                 20                                                       Conversions

                 10

                 0
                      2000 2001 2002 2003 2004 2005 2006 2007 2008 2009
MTBR Before and After
                                   (Population 61 Pumps)
                90
                80
                70
MTBR (Months)




                60
                50
                                                                         Composite MTBR
                40
                                                                         Metal MTBR
                30
                20
                10
                0
                     2000 2001 2002 2003 2004 2005 2006 2007 2008 2009
Overall Average Vibration
                                       (Population 25 Horizontal Pumps)
                          0.20
                          0.18
                          0.16
Overall Vibration (ips)




                          0.14
                          0.12
                          0.10
                          0.08
                          0.06
                          0.04
                          0.02
                          0.00
                                 -12    -6   -1    1    6    12   18    24   30    36   42   48    54
                                        Months Before/After Installation of Composite Wear Rings
Annual Seal Leaks in VOC Service
              (Population of 12 Pumps)
7

6

5

4

3

2

1

0
       Before Composites          After Composites
Specific Examples
Boiler Feed Water
Pump Type          BB3
                   3 Pumps
Operating          230—250 ⁰F
Temperature        (110—120 ⁰C)
Speed              3550 RPM

MTBR Before 15 Months

MTBR After         41 Months*


 * One pump had 3 lube oil system failures which were included in calculation,
 otherwise MTBR would have increased to 163 months
Flare Knockout Drum



             Pump Type     VS7, 4-stages
                           2 Pumps
             Operating     212 ⁰F (100 ⁰C)
             Temperature
             Speed         3550 RPM

             MTBR Before   15 Months

             MTBR After    122+ Months
Gasoline Transfer
        Pump Type     OH2
                      4 Pumps
        Operating     Ambient
        Temperature
        Speed         3550 RPM

        MTBR Before 17 Months

        MTBR After    120 Months
Debutanizer Reflux




            Pump Type     OH2
                          2 Pumps
            Operating     100 ⁰F
            Temperature   (38 ⁰C)
            Speed         3550 RPM
            MTBR Before 22 Months

            MTBR After    107+ Months
Limitations
• In 2005 and 2006 there were some premature
  composite related repairs—failure soon after
  start-up due to mechanical interference from
  reduced clearance
• Pump concentricity standards and checks after
  assembly were improved to address failures
• Vertical pump shaft bushing minimum clearance
  was also adjusted to be 0.002” (0,05 mm) larger
  than 50% of API minimum to avoid assembly
  issues
Conclusions
• Composite upgrade program improved reliability
• Repairs, vibration levels, and seal leaks decreased
• Reducing clearance requires superior
  concentricity
• Previous “bad actors” have run more than 5 years
  with zero failures
• Multi-stage pumps and pumps with start/stop
  operation showed the largest reliability
  improvements

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Long-Term Performance of Composite Wear Rings in Refinery Pumps

  • 1. Evaluating the Long-Term Performance of Composite Wear Rings in Centrifugal Pumps Robert Aronen, Boulden International: Robert Aronen is the Managing Director, EMEA, for Boulden International in Luxembourg. Since 2002, he has been developing the market for the composite material DuPont™ Vespel® CR-6100 in centrifugal pump applications. His prior work includes 4 years as a rotating equipment engineer in the refining industry and 6 years as an engineer for Flowserve, Fluid Sealing Division. Mr. Aronen received a B.S. degree (Mechanical Engineering, 1991) from Rose-Hulman Institute of Technology. Martin Russek, Sunoco: Martin Russek is a Rotating Equipment Reliability Engineer at the Sunoco, Philadelphia Refinery. He has worked in several rotating equipment reliability roles for Sunoco at their 3 refineries in the Northeast since 1999. He has been responsible for numerous pump, compressor, and turbine upgrades. Prior to his work in the refineries, he was a Systems Engineer and Maintenance Engineer for Public Service Electric & Gas Company. He has a Level II vibration certification and is an INPO certified Systems Engineer. Mr. Russek received a B.S. degree (Mechanical Engineering, 1989) from Trenton State College.
  • 2. Background • Refinery instituted a reliability improvement program to install composite wear rings as a standard upgrade to all bad-actor pumps • Initial results were published at 2007 International Pump Users Symposium • This Case Study provides long-term results after more than 4 years of running time
  • 3. Program Scope 61 Centrifugal Pumps Temperatures from 65 ⁰F (17 ⁰C) to 475 ⁰F (246 ⁰C) Hydrocarbon, Acid, Amine, Water, Caustic services Multiple API horizontal and vertical pump types Intermittent (tank farm, product transfer) and continuous process services
  • 4. Which Components? Horizontal Pumps Vertical Pumps Stationary wear rings Stationary wear rings Inter-stage rings Bowl bearings Center-stage bushings Line-shaft bearings Throttle bushings Throat bushings Throat bushings
  • 5. Why Composite Wear Rings? • No metal-to-metal contact – Avoid seizure – Survive process upsets • Reduced Clearance – Lomakin Effect – Lower vibration – Reduced shaft deflection – Lower NPSHR
  • 6. Material Selected: PFA/CF Composite Key Properties Coefficient of thermal expansion (x-y)* 3.1 X 10-6 (in/in/⁰F) ASTM E-831 5.6 X 10-6 (mm/mm/⁰C) Temperature Limit* 500 ⁰F (260 ⁰C) ASTM D-648 Limiting PV* 278000 (psi-ft/min) Falex test 9.7 (Mpa-m/sec) Chemically compatible with everything in the refinery Favorable machining and installation characteristics *Source: DuPont™ Vespel® CR-6100
  • 7. Definitions Repair Any work order—includes seals, bearings, vibration issues, wear ring seizure, inability to make rate, etc… with an associated cost Overall Average of 111 vibration data points from the Vibration 25 horizontal pumps within the study population. LDAR Seal Leak Detection and Repair (LDAR) program, Leaks which monitors single mechanical seals in VOC (volatile organic compound) services.
  • 8. Results from Original Study 2003—2006 Factor Studied Change Number of Repairs 45% Reduction Overall Vibration 25% Reduction LDAR Seal Leaks 70% Reduction *Source: Aronen, R., Boulden, B., and Russek, M., 2007, “Driving Pump Reliability Forward with Advanced Composite Wear Rings,” Proceedings of the 23rd International Pump Users Symposium, Turbomachinery Laboratory, Texas A&M University, College Station, Texas, pp. 15-19.
  • 9. Long Term Results: 2000—2009
  • 10. Annual Repairs (Population 61 Pumps) 60 50 40 Annual Repairs Composite Repairs 30 Metal Repairs 20 Conversions 10 0 2000 2001 2002 2003 2004 2005 2006 2007 2008 2009
  • 11. MTBR Before and After (Population 61 Pumps) 90 80 70 MTBR (Months) 60 50 Composite MTBR 40 Metal MTBR 30 20 10 0 2000 2001 2002 2003 2004 2005 2006 2007 2008 2009
  • 12. Overall Average Vibration (Population 25 Horizontal Pumps) 0.20 0.18 0.16 Overall Vibration (ips) 0.14 0.12 0.10 0.08 0.06 0.04 0.02 0.00 -12 -6 -1 1 6 12 18 24 30 36 42 48 54 Months Before/After Installation of Composite Wear Rings
  • 13. Annual Seal Leaks in VOC Service (Population of 12 Pumps) 7 6 5 4 3 2 1 0 Before Composites After Composites
  • 15. Boiler Feed Water Pump Type BB3 3 Pumps Operating 230—250 ⁰F Temperature (110—120 ⁰C) Speed 3550 RPM MTBR Before 15 Months MTBR After 41 Months* * One pump had 3 lube oil system failures which were included in calculation, otherwise MTBR would have increased to 163 months
  • 16. Flare Knockout Drum Pump Type VS7, 4-stages 2 Pumps Operating 212 ⁰F (100 ⁰C) Temperature Speed 3550 RPM MTBR Before 15 Months MTBR After 122+ Months
  • 17. Gasoline Transfer Pump Type OH2 4 Pumps Operating Ambient Temperature Speed 3550 RPM MTBR Before 17 Months MTBR After 120 Months
  • 18. Debutanizer Reflux Pump Type OH2 2 Pumps Operating 100 ⁰F Temperature (38 ⁰C) Speed 3550 RPM MTBR Before 22 Months MTBR After 107+ Months
  • 19. Limitations • In 2005 and 2006 there were some premature composite related repairs—failure soon after start-up due to mechanical interference from reduced clearance • Pump concentricity standards and checks after assembly were improved to address failures • Vertical pump shaft bushing minimum clearance was also adjusted to be 0.002” (0,05 mm) larger than 50% of API minimum to avoid assembly issues
  • 20. Conclusions • Composite upgrade program improved reliability • Repairs, vibration levels, and seal leaks decreased • Reducing clearance requires superior concentricity • Previous “bad actors” have run more than 5 years with zero failures • Multi-stage pumps and pumps with start/stop operation showed the largest reliability improvements

Editor's Notes

  1. These values are the average values of radial and axial unfiltered readings from all of the horizontal pumps in the study. It is the average overall reading of 111 data points.