HL incident on 2011-02-24 — OK

Operator
Magellan Pipeline Company, Lp
Cause
Material Failure Of Pipe Or Weld
Commodity
Refined And/or Petroleum Product (Non-Hvl) Which Is A Liquid At Ambient Conditions
Program
HL
Damage and Injuries
0 fatalities 0 injuries
Property damage (nominal)
$403,000
Incident datetime
2011-02-24 01:03
Report number
Location
OK
Narrative
The pipeline was operating at steady state prior to the event at approximately 10,000 bph. No abnormal operating conditions occurred immediately prior to the event. The pipeline controller via scada received an alert of high flowrate and low discharge pressure. The pipeline was promptly shutdown and remotely operated valves closed. Upon investigation it was discovered that pipeline long seam had split on top of the pipe. Further metalurgical analysis determined it was a damaged skelp edge during manufacturing that caused a lack of bonding. - see analysis attached. Removed part a #10 as instructed by email of piyali talukdar on 2/28/13. Supplemental/final (02/11/2020) updated g5-1 to remove "under investigation"
Detailed record list
Report Received Date
2011-03-25 00:00:00
Iyear
2011
Report Number
20110105
Supplemental Number
33319
Report Type
Supplemental Final
Operator Id
Name
Magellan Pipeline Company, Lp
Operator Street Address
100 West 5th Street
Operator City Name
Tulsa
Operator State Abbreviation
OK
Operator Postal Code
74103
Local Datetime
2011-02-24 01:03:00
Location Latitude
Location Longitude
Commodity Released Type
Refined And/or Petroleum Product (Non-Hvl) Which Is A Liquid At Ambient Conditions
Commodity Subtype
Gasoline (Non-Ethanol)
Unintentional Release Bbls
482
Recovered Bbls
50
Fatality Ind
No
Fatal
0
Injury Ind
No
Injure
0
Accident Identifier
Cpm Leak Detection System Or Scada-Based Information (Such As Alarm(S), Alert(S), Event(S), And/or Volume Calculations)
Incident Identified Datetime
2011-02-24 01:03:00
System Part Involved
Onshore Pipeline, Including Valve Sites
On Off Shore
Onshore
Shutdown Due Accident Ind
Yes
Shutdown Datetime
2011-02-24 01:03:00
Restart Datetime
2011-02-28 07:30:00
On Site Datetime
2011-02-24 01:27:00
Nrc Rpt Datetime
2011-02-24 02:26:00
Nrc Rpt Num
Ignite Ind
No
Explode Ind
No
Upstream Valve Type Ind
Automatic
Downstream Valve Type Ind
Automatic
Num Pub Evacuated
30
Pipe Fac Name
Texas City To Pasadena 18" Product Line
Segment Name
7005
Onshore State Abbreviation
Tx
Onshore Postal Code
77590
Onshore City Name
Texas City
Onshore County Name
Galveston
Designated Location
Survey Station No.
Designated Name
146+24
Federal
No
Location Type
Pipeline Right-Of-Way
Incident Area Type
Underground
Incident Area Subtype
Under Soil
Depth Of Cover
49
Crossing
No
Pipe Facility Type
Interstate
Item Involved
Pipe
Pipe Type
Pipe Seam
Pipe Diameter
18
Pipe Wall Thickness
0.219
Pipe Smys
52000
Pipe Specification
Api 5l X52
Pipe Seam Type
Erw - Low Frequency
Pipe Manufacturer
Youngstown
Pipe Coating Type
Coal Tar
Installation Year
1962
Manufactured Year
1962
Material Involved
Carbon Steel
Release Type
Rupture
Rupture Orient
Longitudinal
Rupture Width
3.5
Rupture Length
35.7
Wildlife Impact Ind
No
Soil Contamination
Yes
Long Term Assessment
No
Remediation Ind
No
Water Contam Ind
Yes
Surface Contam Ind
Yes
Amount Released
0.48
Rel Water Name
Pierrebayou
Could Be Hca
Yes
Commodity Reached Hca
Yes
Other Pop Ind
Yes
Other Pop Yes No
Yes
Usa Drinking Ind
Yes
Usa Drinking Yes No
Yes
Est Cost Oper Paid
0
Est Cost Gas Released
60817
Est Cost Prop Damage
403000
Est Cost Emergency
149000
Est Cost Environmental
1777200
Est Cost Other
0
Prpty
2390017
Accident Psig
767
Mop Psig
840
Accident Pressure
Pressure Did Not Exceed Mop
Pressure Restriction Ind
No
Length Segment Isolated
21149
Internal Inspection Ind
Yes
Operation Complications Ind
No
Pipeline Function
> 20% Smys Regulated Transmission
Scada In Place Ind
Yes
Scada Operating Ind
Yes
Scada Functional Ind
Yes
Scada Detection Ind
Yes
Scada Conf Ind
Yes
Cpm In Place Ind
Yes
Cpm Operating Ind
Yes
Cpm Functional Ind
Yes
Cpm Detection Ind
Yes
Cpm Conf Ind
Yes
Investigation Status
Yes, but the investigation of the control room and/or controller actions has not yet been completed by the operator (supplemental report required)
Employee Drug Test Ind
Yes
Contractor Drug Test Ind
No
Num Employees Tested
1
Num Employees Failed
0
Cause
Material Failure Of Pipe Or Weld
Cause Details
Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Field Exam Ind
Yes
Failure Type
Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Other Factor
Yes
Other Factor Details
Damaged Skelp Edge During Manufacturing - See Analysis
Additional Lack Fusion Ind
Yes
Collected Data Ind
Yes
Axial Magnetic Flx Lkg Ind
Yes
Cir Trn Wave Mgn Flx Lkg Ind
Yes
Geometry Deformation Ind
Yes
Emat Ind
Yes
Axial Recent Year
2004
Circ Wave Recent Year
2009
Geometry Recent Year
2009
Emat Recent Year
2010
Has Hydrtst Conduc Before Ind
Yes
Hydrtst Most Rcnt Year
1990
Hydrtst Most Rcnt Pressure
1140
Direct Asmnt Conducted
No
Non Destructive Exam Ind
No
Preparer Name
D******* C*********
Preparer Email
D******************@m*********.com
Prepared Date
2020-02-11 00:00:00
Authorizer Name
D******* C*********
Authorizer Telephone
918-574-7386
Authorizer Title
Compliance Coordinator Sr
Authorizer Email
D******************@m*********.com
Narrative
The pipeline was operating at steady state prior to the event at approximately 10,000 bph. No abnormal operating conditions occurred immediately prior to the event. The pipeline controller via scada received an alert of high flowrate and low discharge pressure. The pipeline was promptly shutdown and remotely operated valves closed. Upon investigation it was discovered that pipeline long seam had split on top of the pipe. Further metalurgical analysis determined it was a damaged skelp edge during manufacturing that caused a lack of bonding. - see analysis attached. Removed part a #10 as instructed by email of piyali talukdar on 2/28/13. Supplemental/final (02/11/2020) updated g5-1 to remove "under investigation"
Report Received Date 2011-03-25 00:00:00
Iyear 2011
Report Number 20110105
Supplemental Number 33319
Report Type Supplemental Final
Operator Id 22610 PHMSA Enforcement
Name Magellan Pipeline Company, Lp
Operator Street Address 100 West 5th Street
Operator City Name Tulsa
Operator State Abbreviation OK
Operator Postal Code 74103
Local Datetime 2011-02-24 01:03:00
Location Latitude 29.4009 Google Maps OpenStreetMap
Location Longitude -94.95689 Google Maps OpenStreetMap
Commodity Released Type Refined And/or Petroleum Product (Non-Hvl) Which Is A Liquid At Ambient Conditions
Commodity Subtype Gasoline (Non-Ethanol)
Unintentional Release Bbls 482
Recovered Bbls 50
Fatality Ind No
Fatal 0
Injury Ind No
Injure 0
Accident Identifier Cpm Leak Detection System Or Scada-Based Information (Such As Alarm(S), Alert(S), Event(S), And/or Volume Calculations)
Incident Identified Datetime 2011-02-24 01:03:00
System Part Involved Onshore Pipeline, Including Valve Sites
On Off Shore Onshore
Shutdown Due Accident Ind Yes
Shutdown Datetime 2011-02-24 01:03:00
Restart Datetime 2011-02-28 07:30:00
On Site Datetime 2011-02-24 01:27:00
Nrc Rpt Datetime 2011-02-24 02:26:00
Nrc Rpt Num 968387 NRC Report How to search
Ignite Ind No
Explode Ind No
Upstream Valve Type Ind Automatic
Downstream Valve Type Ind Automatic
Num Pub Evacuated 30
Pipe Fac Name Texas City To Pasadena 18" Product Line
Segment Name 7005
Onshore State Abbreviation Tx
Onshore Postal Code 77590
Onshore City Name Texas City
Onshore County Name Galveston
Designated Location Survey Station No.
Designated Name 146+24
Federal No
Location Type Pipeline Right-Of-Way
Incident Area Type Underground
Incident Area Subtype Under Soil
Depth Of Cover 49
Crossing No
Pipe Facility Type Interstate
Item Involved Pipe
Pipe Type Pipe Seam
Pipe Diameter 18
Pipe Wall Thickness 0.219
Pipe Smys 52000
Pipe Specification Api 5l X52
Pipe Seam Type Erw - Low Frequency
Pipe Manufacturer Youngstown
Pipe Coating Type Coal Tar
Installation Year 1962
Manufactured Year 1962
Material Involved Carbon Steel
Release Type Rupture
Rupture Orient Longitudinal
Rupture Width 3.5
Rupture Length 35.7
Wildlife Impact Ind No
Soil Contamination Yes
Long Term Assessment No
Remediation Ind No
Water Contam Ind Yes
Surface Contam Ind Yes
Amount Released 0.48
Rel Water Name Pierrebayou
Could Be Hca Yes
Commodity Reached Hca Yes
Other Pop Ind Yes
Other Pop Yes No Yes
Usa Drinking Ind Yes
Usa Drinking Yes No Yes
Est Cost Oper Paid 0
Est Cost Gas Released 60817
Est Cost Prop Damage 403000
Est Cost Emergency 149000
Est Cost Environmental 1777200
Est Cost Other 0
Prpty 2390017
Accident Psig 767
Mop Psig 840
Accident Pressure Pressure Did Not Exceed Mop
Pressure Restriction Ind No
Length Segment Isolated 21149
Internal Inspection Ind Yes
Operation Complications Ind No
Pipeline Function > 20% Smys Regulated Transmission
Scada In Place Ind Yes
Scada Operating Ind Yes
Scada Functional Ind Yes
Scada Detection Ind Yes
Scada Conf Ind Yes
Cpm In Place Ind Yes
Cpm Operating Ind Yes
Cpm Functional Ind Yes
Cpm Detection Ind Yes
Cpm Conf Ind Yes
Investigation Status Yes, but the investigation of the control room and/or controller actions has not yet been completed by the operator (supplemental report required)
Employee Drug Test Ind Yes
Contractor Drug Test Ind No
Num Employees Tested 1
Num Employees Failed 0
Cause Material Failure Of Pipe Or Weld
Cause Details Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Field Exam Ind Yes
Failure Type Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Other Factor Yes
Other Factor Details Damaged Skelp Edge During Manufacturing - See Analysis
Additional Lack Fusion Ind Yes
Collected Data Ind Yes
Axial Magnetic Flx Lkg Ind Yes
Cir Trn Wave Mgn Flx Lkg Ind Yes
Geometry Deformation Ind Yes
Emat Ind Yes
Axial Recent Year 2004
Circ Wave Recent Year 2009
Geometry Recent Year 2009
Emat Recent Year 2010
Has Hydrtst Conduc Before Ind Yes
Hydrtst Most Rcnt Year 1990
Hydrtst Most Rcnt Pressure 1140
Direct Asmnt Conducted No
Non Destructive Exam Ind No
Preparer Name D******* C*********
Preparer Email D******************@m*********.com
Prepared Date 2020-02-11 00:00:00
Authorizer Name D******* C*********
Authorizer Telephone 918-574-7386
Authorizer Title Compliance Coordinator Sr
Authorizer Email D******************@m*********.com
Narrative The pipeline was operating at steady state prior to the event at approximately 10,000 bph. No abnormal operating conditions occurred immediately prior to the event. The pipeline controller via scada received an alert of high flowrate and low discharge pressure. The pipeline was promptly shutdown and remotely operated valves closed. Upon investigation it was discovered that pipeline long seam had split on top of the pipe. Further metalurgical analysis determined it was a damaged skelp edge during manufacturing that caused a lack of bonding. - see analysis attached. Removed part a #10 as instructed by email of piyali talukdar on 2/28/13. Supplemental/final (02/11/2020) updated g5-1 to remove "under investigation"

All rights reserved. Copyright © by ClearPHMSA