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RCFA Case Study: Infant Mortality: Lean Solvent Centrifugal Pump Motor DELIVERING ENERGY TO THE WORLD Qadeer Ahmed Sr. Reliability Engineer, Integrity & Reliability Engineering Qatargas Operating Company Limited, Qatar The 1 st Middle East Turbomachinery Symposium (METS) February 13 - 16, 2011 Sheraton Resort and Convention Center - Doha, Qatar
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Page 1: RCFA Case Study - CORE

RCFA Case Study: Infant Mortality: Lean Solvent Centrifugal Pump Motor

DELIVERING ENERGY TO THE WORLD

Qadeer Ahmed Sr. Reliability Engineer, Integrity & Reliability Engineering

Qatargas Operating Company Limited, Qatar

The 1st Middle East Turbomachinery Symposium (METS)February 13 - 16, 2011

Sheraton Resort and Convention Center - Doha, Qatar

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DELIVERING LNG TO THE WORLD

Agenda:

• Introduction:

• Qatargas Operating Company Limited

• Refresher: Bathtub Curve & Failure Regions (i.e. Infant Mortality)

• Root Cause & Failure Analysis

• Brief Introduction – Incident and Action Plan

• Simplified System Diagram

• Basic Data – Pump & Motor

• Event Diagram (Timeline)

• Pictures of Failed Parts

• PROACT Logic Tree & Vibration Data

• Root Cause(s)

• Recommendations & Lesson Learned

• Q&A / Thanks

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Introduction

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• Qatargas is pioneer in Qatar’s LNG production and will be the largest producer of LNG in the world by 2010 with total production of 77 MTPA.

• Qatargas existing LNG capacity is approx 25.6 MTPA of LNG

• Qatargas is going through phenomenal expansion and capacity will be

42 MTPA of LNG by end of 2010

• Qatargas Expansion Projects – 4 new Mega Trains (7.8 MTPA) : TR4&5 in production – Largest LNG Trains

– Laffan Refinery (150K BPD): Naphta, Kerosene, Gasoil

– Common Sulfur Project (12K TPD) – Granulated Sulfur

– Q-Max & Q- Flex LNG Ships (Q-Flex:210,000 m3 and Q-Max:266,000 m3)

• High Availability & Reliability is a vital to meet global demand– Asset Management is key to achieve desired Reliability & Availability

Introduction:

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A Glimpse - Qatargas Offshore:

LNG TRAIN 5

QATARGAS NFBCOMPLEX

LNG TRAIN 4

PU

WH4 - 64 m

(12 Slots)

QatargasRas Laffan Industrial City

PL4

34”

(91 km)

Power/Comm

5-6 Power/Comm5-4

QATARGAS NFB COMPLEX

WH6 - 56 m

(15 Slots)

WH5 - 46 m

(15 Slots)

PL5-6

16”

(800 m)

PL5-4

16”

(300 m)

Power/Comm

Main

FOC

to

Shore

PL6

38”

(81 km)

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A Glimpse - Qatargas Onshore:

LNG Tanks

CSP

Liquids Loading

Berths

QG2 TR4 & 5

QG3TR6 &

QG4TR7

Laffan Refinery

QG1

Liquid Storage

LNG Loading Berths

~150,000 BPD

12,000 TPD

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Basics: Refresher!!

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What is Bathtub Curve?

• Bathtub Curve– It is a Reliability Engineering tool which describe the particular form of

Hazard Rate. Lifetime of a population of product in graphical representation. The bathtub curve mainly consist of three regions:

– Infant Mortality/Early Failure:

• It is a decreasing failure rate region in the curve mainly constitutes of early failures.

– Random Failures Region (Useful Life):

• It is a constant failure rate region in the curve mainly constitutes of random failures

– Wear Out / Aging :

• It is a increasing failure rate region in the curve mainly constitutes of wear out / aged failures

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Bathtub Curve:

Source: http://en.wikipedia.org

Most Critical Region

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RCFA

(Root Cause Failure Analysis)

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Incident Description:

• Description:

• During the early stage of plant service, Two out of two motors failed within a

short duration and caused disruption in normal operations and other

consequential damages (pump, production etc..)

• Action Plan:

• RCFA investigation was requested using Meridium PROACT

• RCFA team was established (SMEs, Vendor, EPC invited)

• RCFA Charter & Critical Success Factors were developed

• All the events were collected in Meridium Event Manager

• All the evidences and required data collected

• All pictures, failure data, Trends and failed parts were analyzed

• PROACT Logic Tree was developed with Failure Modes and Hypotheses

• Root Cause Identified & Issued Recommendations

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Simplified System Diagram:

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Pump & Motor Basic Data:

Driver: Motor

• Type: Induction Motor

• Voltage: 6.6 KV

• Rated Output: 185 KW

• Rated Torque: 593 NM

• Speed: 3000 RPM

• Bearings

– Radial: Ball

• Lubrication: Grease

Driven: Pump

• Type: Centrifugal

• No. of Stages: 2

• Rated Capacity: 257 M3/HR

• Liquid: Lean Solvent

• Bearings

– Radial: Sleeve

– Thrust: Ball

• Lubrication: Oil Ring

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Event Diagram (Timeline):

DELIVERING LNG TO THE WORLD

Motor B Tripped

16/02

Motor A Started

Unit was running

at 87% load

23/02

Vibration Alarm

Appeared &

Attended

23/02

23/02

Motor A tripped on

Thermal O/L Protection

Low Flow Alarm &

Unit Tripped on

Level Protection

23/02

Noticed smoke in

the area (motor),

EMS notified

23/02

23/02

Called Electrical

Mtce to check

motor

Motor was checked, found

shaft jammed – Winding

Resistance /Insulation

Resistance Satisfactory

Motors Inspected :

Found Bearings &

Shaft Damaged

23/0223/02

Incident

Incident

1

2 3

4

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Pictures - Failed Bearings:

Motor Drive End

Motor Non Drive End

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Pictures - Burnt Rotor Shaft:

Motor Burnt Shaft

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Pictures - Burnt Stator / Rotor:

Cage - Drive End

Stator - Drive End

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Consequential Damage:

• Internal Coating Peeled Off

• Lube Oil Contamination

Pump BearingPeeled Off Coating

• Bearing Damage (Replaced)

• Excessive Clearance

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PROACT Logic Tree:

Failure Modes

Incident

Hypotheses

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Verifications - Vibration Trends

Motor & Pump

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Vibration Trend – Overall:

Overall Vibration Trends

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Spectrum – Pump:

Pump Drive End

Pump Non Drive End

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Spectrum – Motor Drive End:

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Leading & Contributing Cause(s):

Leading Cause:

Lack of lubrication is the leading root cause of this failure. No grease was

found during inspection and bearing showed the clear signs of overheating.

Vibration data supports and confirms the failure initiating point was bearing

(BPFO -Ball Pass Frequency Outer Race).

Contributors:

PMs to lubricate the bearings were not active in CMMS.

Grease was not checked/replaced during commissioning (built in 2006).

Greasing procedure was not available for such motors

Vendor Recommendation were not followed about greasing.

DELIVERING LNG TO THE WORLD24

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Recommendations & Lessons Learned:

Recommendations:

1. Activate the all PM plans in CMMS. Ensure to set the initial PM startup date

manually. Revisit the equipment strategies to include vendor recommendations.

2. Create area based lubrication work orders and release for maintenance execution.

3. Develop greasing procedure for Motors (based on type of bearing).

4. Inspect the pump and accessories prior to installation of new motor.

Lessons Learned:

1. The Project Maintenance & Engineering was informed immediately to take

appropriate measures to address similar potential issues.

2. The new project practices were issued. Check sheets were developed to ensure

proper lubrication before the mechanical run test to avoid such failures. (No reported

bearing failure)

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Q & A ….

Thanks!!!

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