Amr Mohamed Gadpump casing for boiler feed water service led to major damage. of casing inner walls...
Transcript of Amr Mohamed Gadpump casing for boiler feed water service led to major damage. of casing inner walls...
Presenter
Amr Mohamed Gad
Senior Machinery Engineer with RasGas company since 2007
• 13 years of experience in maintenance, retrofits, and upgrades of Gas Turbines, Compressors and Pumps in natural gas facilities.
• Previous publications at 5 major worldwide conferences
Boiler Feed Water Pumps Performance Loss
Amr Mohamed Gad– RasGasDr.Nicholas White – RasGas
Arbain Bin Mahmood– RasGas
2nd Middle East Turbo Machinery Symposium 17th – 21st March 2013
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Index
• RGX2 Steam Condensate System
• Problem Summary
• Troubleshooting History
• Unit 92-A261A –Failure
• Performance Deterioration
• RCFA-Unit 92-P261A
• Operational Risk Mitigation
• Recommendations Results
• Lessons Learned
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RGX2 Steam Condensate System
x6 No. BFW
Steam condensate system set up at RGX2• Total of x6 Boiler Feed Water Pumps (x4 steam driven pumps and
x2 motor driven pumps).
Operating philosophy N+2:• x4 in service and x2 Stand by operation.
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RGX2 Steam Condensate System
Pump specifications:
• Rated capacity 750 M3/hr
• Rated power 1.7 MW
• Differential head 680m
• Horizontally split casing
• 4 stage with double inlet impeller
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RGX2 Steam Condensate System
New pump before installation Old pump at skid in RGX2
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Problem Summary
• One pump experienced high thrust bearing temperature alarm after 16 months of operation
• The thrust bearing was replaced twice during the following 6 months without identifying the root cause
• System operation indicated low pump performance (flow rate and head rise)
• During the 25 months of operation, thrust bearing temperature again reached high alarm level and pump was found seized upon inspection
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Troubleshooting History
Historical RecordsUnit 92-P261A historical events shown on a timeline
92P261A PMP NDE BRG TEMP92P261A PMP NDE BRG TEMP92P261B PMP NDE BRG TEMP92P261B PMP NDE BRG TEMP92P261A PMP NDE BRG TEMP92P261A PMP NDE BRG TEMP92P261B PMP NDE BRG TEMP92P261B PMP NDE BRG TEMPOIL TO PMP & TURB 92P261AWB FR 92P261ABCDWB FR 92P261ABCD
92TI6864AA.PV
92TI6864AB.PV
92TI6864BA.PV
92TI6864BB.PV
92TI6865AA.PV
92TI6865AB.PV
92TI6865BA.PV
92TI6865BB.PV
92PI6802A.PV
92PI6517.PV
92PI6518.PV
Plot-0
10/6/2009 8:20:59.518 AM 10/13/2010 8:20:59.518 AM372.00 days
20
40
60
80
100
0
120
61.994
61.984
7.4481E-02
75.849
74.042
29.695
32.43
58.462
65.055
28.376
32.137
pump’s thrust bearing temperature increase due to bearing degradation over one year – alarm level reach xx deg C
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Troubleshooting History
\\RTIS67\92VI6808AA.P12.015UM PP\\RTIS67\92VI6808AB.P11.233UM PP\\RTIS67\92VI6809AA.P20.928UM PP\\RTIS67\92VI6809AB.P25.958UM PP\\RTIS67\92VI6810AA.P8.1319UM PP\\RTIS67\92VI6810AB.P8.1319UM PP\\RTIS67\92VI6810BA.P6.2027UM PP\\RTIS67\92VI6811AA.P8.9133UM PP\\RTIS67\92VI6811AB.P7.7411UM PP
92P261A PMP NDE VIB X92P261A PMP NDE VIB Y92P261A PMP DE VIB X92P261A PMP DE VIB Y92P261A TURB DE VIB X92P261A TURB DE VIB Y92P261ABTURB DE VIB X92P261A TURB NDE VIB X
2/8/2012 7:45:30.806 AM2/1/2012 7:45:40.602 AM 7.00 days
Plot-0
4
9
14
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24
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2/1/2012 4:39:46 PM
11.62410.84218.60825.5928.13198.13196.20278.91337.3748
2/7/2012 5:34:00 PM
11.62411.23321.31926.3498.13197.74115.03058.91337.3748
Unit 92-P261A -Vibration readings
Pump D.E
radial vibration
Pump N.D.E
radial vibration
Turbine D.E & N.D.E
radial vibration
Pump D.E/N.D.E VAH&VAHH is 50/70 Mm PK-PK
Turbine D.E/N.D.E VAH&VAHH is 25/37 Mm PK-PK
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Unit 92-A261A –Failure
Scoring and smear on thrust pads Smeared Journal pads
Thrust Bearing failure signs:
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Unit 92-A261A –Failure
Cavitation damage
Cavitation damage on 1st stage
Casing erosion
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Unit 92-A261A –Failure
Casing erosion
RCFA initiated August 2011 and completed October 2011
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Performance Deterioration
Optimum performance Deteriorated performance Other pumps performance
Pump A
Other
5
pumps
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RCFA-Unit 92-P261A
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RCFA-Unit 92-P261A
RCFA – Findings
• Root Cause (Human) - Incorrect material specification of the pump casing for boiler feed water service led to major damageof casing inner walls and rotor parts
• Contributing Factor 1 (Latent) – Insufficient online monitoring of pump performance due to inadequate instrumentation prevented effective pump health monitoring
• Contributing Factor 2 (Latent) – Inadequate surveillance program for boiler feed water conditions led to a possible corrosive environment within pump flow path
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RCFA-Unit 92-P261A
RCFA – Recommendations
• Immediate action: Purchase x6 new BFWPs with 12%Cr Stainless Steel casings and replace the existing pumps with carbon steel casing
• Medium action: Revise the Equipment Strategy to perform a bi-monthly online performance monitoring task including steam condensate dissolved oxygen and pH levels to ensure they remain within specification
• Long term action: Improve online monitoring by installation of the following:-Digital discharge pressure transmitter-Install flow measurement devices on the discharge and recirculation line
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Operational Risk Mitigation
Recovery TEAM
Rotating Machinery Eng.
Maintenance Process Eng.
Manufacturing Dep.
Contracts Dep.
Supply Dep.
Electrical and Instrumentation Eng.
Asset Management
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Operational Risk Mitigation
Integrated Repair plan• x3 pumps repaired between October 2011 and March 2012• x2 pumps were repaired used spare parts manufactured by
third party as fast track repair to save time
• System reviewed for equipment reliability (Turbines, Automatic Recycle Valves, Instruments etc.) and corrective actions taken as appropriate
• Close monitoring and measurement of discharge and recycle flow using clamp flow meter to assess pump performance
• Long term - Installation of x6 new BFW pumps with stainless steel casing (procurement and installation during 14 months)
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Recommendations Results
• Performance for the repaired 3 units as interim solution was
similar to OEM design.
• Ultimate replacement of all pumps by new stainless steel
casing's units results in operating the BFW system with reliable
units as per OEM design.
Optimum performance
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Lessons Learned
• Follow API610 guidelines during equipment procurement(material specifications versus fluid service)
• Improve datasheet and specification review during project FEED and procurement
• Improve online monitoring instruments required during plant design
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Questions?
Authors:
Amr Mohamed Gad – RasGas
Dr. Nicholas White - RasGas
Arbain Mahmood – RasGas
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Backup
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23 | RasGas classification/title heading | December 12
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Operational Risk Mitigation
Integrated Repair plan
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