HL incident on 2015-09-16 — TX

Operator
Shell Pipeline Co., L.p.
Cause
Material Failure Of Pipe Or Weld
Commodity
Crude Oil
Program
HL
Damage and Injuries
0 fatalities 0 injuries
Property damage (nominal)
$300,000
Incident datetime
2015-09-16 21:34
Report number
Location
TX
Narrative
During a set point increase of three pounds of discharge pressure at an intermediate pump station by the controller, the pipe section approx. 0.5 miles downstream ruptured. The controller immediately identified the release by the pump station increased flow rate and low suction shutdown of the pump station. The controller took immediate action to shutdown the entire pipeline and closing intermediate block valves. The controller then closed off the receiving location to reduce the release of crude oil. The controllers actions from the time of the low suction shutdown of the pump station unit to the shutdown of the pipeline system was two minutes. This is faster than the cpm system can identify a release. The controller then contacted the local & on call supervisors, the controller console supervisor to inform them of his actions. The local supervisor called out two personnel to begin looking for the release site. Timing was after dark with limited visibility. The personnel drove the area north of the pump station. The topography is rolling hills and pasture land with limited access. They did not see the release site where they were able to drive. The air patrol was called to be over the pump station and head north at first light. The air patrol identified the location at 07:05 hrs. Metallurgical examination report - "the pipe section ruptured at a preexisting fatigue crack. The fatigue crack initiated from small corrosion pits along the internal surface at the toe of the longitudinal seam weld. Evidence of interlinked inclusions were observed, along with a stepwise fracture morphology, suggesting that stress-oriented hydrogen inducted cracking (sohic) may have contributed to the failure." 10/24/16 updated manufacturer armco 1982 & sub-cause original manufacturing-related.
Detailed record list
Report Received Date
2015-10-14 00:00:00
Iyear
2015
Report Number
20150364
Supplemental Number
21783
Report Type
Supplemental Final
Operator Id
Name
Shell Pipeline Co., L.p.
Operator Street Address
150 North Dairy Ashford Road Wck Bldg. A
Operator City Name
Houston
Operator State Abbreviation
TX
Operator Postal Code
77079
Local Datetime
2015-09-16 21:34:00
Location Latitude
Location Longitude
Commodity Released Type
Crude Oil
Unintentional Release Bbls
900
Intentional Release Bbls
0
Recovered Bbls
800
Fatality Ind
No
Fatal
0
Injury Ind
No
Injure
0
Accident Identifier
Controller
Operator Type
Operator Employee
Incident Identified Datetime
2015-09-16 21:34:00
System Part Involved
Onshore Pipeline, Including Valve Sites
On Off Shore
Onshore
Shutdown Due Accident Ind
Yes
Shutdown Datetime
2015-09-16 21:36:00
Restart Datetime
2015-09-21 19:45:00
On Site Datetime
2015-09-17 07:30:00
Nrc Rpt Datetime
2015-09-17 08:02:00
Nrc Rpt Num
Ignite Ind
No
Explode Ind
No
Upstream Valve Type Ind
Remotely Controlled
Downstream Valve Type Ind
Remotely Controlled
Num Pub Evacuated
0
Pipe Fac Name
North 20 - Coalinga To Avon
Segment Name
Tracy To Marsh Creek
Onshore State Abbreviation
Ca
Onshore Postal Code
95304
Onshore City Name
Tracy
Onshore County Name
San Joaquin
Designated Location
Milepost/valve Station
Designated Name
137
Federal
No
Location Type
Pipeline Right-Of-Way
Incident Area Type
Underground
Incident Area Subtype
Under Soil
Depth Of Cover
60
Crossing
No
Pipe Facility Type
Intrastate
Item Involved
Pipe
Pipe Type
Pipe Body
Pipe Diameter
24
Pipe Wall Thickness
0.26
Pipe Smys
60000
Pipe Specification
5l- X60
Pipe Seam Type
Dsaw
Pipe Manufacturer
Armco
Pipe Coating Type
Polyolefin
Installation Year
1989
Manufactured Year
1982
Material Involved
Carbon Steel
Release Type
Rupture
Rupture Orient
Longitudinal
Rupture Width
6
Rupture Length
36
Wildlife Impact Ind
No
Soil Contamination
Yes
Long Term Assessment
No
Remediation Ind
No
Water Contam Ind
No
Could Be Hca
Yes
Commodity Reached Hca
Yes
Usa Drinking Ind
Yes
Usa Drinking Yes No
Yes
Usa Ecological Ind
Yes
Usa Ecological Yes No
Yes
Est Cost Oper Paid
0
Est Cost Gas Released
0
Est Cost Prop Damage
300000
Est Cost Emergency
900000
Est Cost Environmental
0
Est Cost Other
0
Prpty
1200000
Accident Psig
878
Mop Psig
936
Accident Pressure
Pressure Did Not Exceed Mop
Pressure Restriction Ind
No
Length Segment Isolated
16125
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
No
Cpm In Place Ind
Yes
Cpm Operating Ind
Yes
Cpm Functional Ind
Yes
Cpm Detection Ind
No
Cpm Conf Ind
No
Investigation Status
Yes, specify investigation result(s): (select all that apply)
Invest No Schedule Ind
Yes
Invest No Schedule Ind Details
The Investigation Did Not Reveal Any Fatigue Issues Since The Controller's Actions Were Deemed Appropriate For The Incident.
Invest No Control Room Ind
Yes
Invest No Controller Ind
Yes
Employee Drug Test Ind
No
Contractor Drug Test Ind
No
Cause
Material Failure Of Pipe Or Weld
Cause Details
Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Metallurgical Ind
Yes
Failure Type
Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Fatigue Vibr Related
Yes
Failure Subtype
Mechanically-Induced Fatigue Prior To Installation (Such As During Transport Of Pipe)
Additional Crack Ind
Yes
Collected Data Ind
Yes
Axial Magnetic Flx Lkg Ind
Yes
Geometry Deformation Ind
Yes
Axial Recent Year
2013
Geometry Recent Year
2013
Has Hydrtst Conduc Before Ind
No
Direct Asmnt Conducted
No
Non Destructive Exam Ind
No
Preparer Name
R****** K*****
Preparer Title
Regulatory Specialist
Preparer Email
R*************@s****.com
Preparer Telephone
713 241 1064
Preparer Fax
713 241 8498
Prepared Date
2016-10-24 00:00:00
Authorizer Name
D****** P****
Authorizer Telephone
713 241 2035
Authorizer Title
Integrity Regulatory Srvc Manager
Authorizer Email
D************@s****.com
Narrative
During a set point increase of three pounds of discharge pressure at an intermediate pump station by the controller, the pipe section approx. 0.5 miles downstream ruptured. The controller immediately identified the release by the pump station increased flow rate and low suction shutdown of the pump station. The controller took immediate action to shutdown the entire pipeline and closing intermediate block valves. The controller then closed off the receiving location to reduce the release of crude oil. The controllers actions from the time of the low suction shutdown of the pump station unit to the shutdown of the pipeline system was two minutes. This is faster than the cpm system can identify a release. The controller then contacted the local & on call supervisors, the controller console supervisor to inform them of his actions. The local supervisor called out two personnel to begin looking for the release site. Timing was after dark with limited visibility. The personnel drove the area north of the pump station. The topography is rolling hills and pasture land with limited access. They did not see the release site where they were able to drive. The air patrol was called to be over the pump station and head north at first light. The air patrol identified the location at 07:05 hrs. Metallurgical examination report - "the pipe section ruptured at a preexisting fatigue crack. The fatigue crack initiated from small corrosion pits along the internal surface at the toe of the longitudinal seam weld. Evidence of interlinked inclusions were observed, along with a stepwise fracture morphology, suggesting that stress-oriented hydrogen inducted cracking (sohic) may have contributed to the failure." 10/24/16 updated manufacturer armco 1982 & sub-cause original manufacturing-related.
Report Received Date 2015-10-14 00:00:00
Iyear 2015
Report Number 20150364
Supplemental Number 21783
Report Type Supplemental Final
Operator Id 31174 PHMSA Enforcement
Name Shell Pipeline Co., L.p.
Operator Street Address 150 North Dairy Ashford Road Wck Bldg. A
Operator City Name Houston
Operator State Abbreviation TX
Operator Postal Code 77079
Local Datetime 2015-09-16 21:34:00
Location Latitude 37.72575 Google Maps OpenStreetMap
Location Longitude -121.55485 Google Maps OpenStreetMap
Commodity Released Type Crude Oil
Unintentional Release Bbls 900
Intentional Release Bbls 0
Recovered Bbls 800
Fatality Ind No
Fatal 0
Injury Ind No
Injure 0
Accident Identifier Controller
Operator Type Operator Employee
Incident Identified Datetime 2015-09-16 21:34:00
System Part Involved Onshore Pipeline, Including Valve Sites
On Off Shore Onshore
Shutdown Due Accident Ind Yes
Shutdown Datetime 2015-09-16 21:36:00
Restart Datetime 2015-09-21 19:45:00
On Site Datetime 2015-09-17 07:30:00
Nrc Rpt Datetime 2015-09-17 08:02:00
Nrc Rpt Num 1128712 NRC Report How to search
Ignite Ind No
Explode Ind No
Upstream Valve Type Ind Remotely Controlled
Downstream Valve Type Ind Remotely Controlled
Num Pub Evacuated 0
Pipe Fac Name North 20 - Coalinga To Avon
Segment Name Tracy To Marsh Creek
Onshore State Abbreviation Ca
Onshore Postal Code 95304
Onshore City Name Tracy
Onshore County Name San Joaquin
Designated Location Milepost/valve Station
Designated Name 137
Federal No
Location Type Pipeline Right-Of-Way
Incident Area Type Underground
Incident Area Subtype Under Soil
Depth Of Cover 60
Crossing No
Pipe Facility Type Intrastate
Item Involved Pipe
Pipe Type Pipe Body
Pipe Diameter 24
Pipe Wall Thickness 0.26
Pipe Smys 60000
Pipe Specification 5l- X60
Pipe Seam Type Dsaw
Pipe Manufacturer Armco
Pipe Coating Type Polyolefin
Installation Year 1989
Manufactured Year 1982
Material Involved Carbon Steel
Release Type Rupture
Rupture Orient Longitudinal
Rupture Width 6
Rupture Length 36
Wildlife Impact Ind No
Soil Contamination Yes
Long Term Assessment No
Remediation Ind No
Water Contam Ind No
Could Be Hca Yes
Commodity Reached Hca Yes
Usa Drinking Ind Yes
Usa Drinking Yes No Yes
Usa Ecological Ind Yes
Usa Ecological Yes No Yes
Est Cost Oper Paid 0
Est Cost Gas Released 0
Est Cost Prop Damage 300000
Est Cost Emergency 900000
Est Cost Environmental 0
Est Cost Other 0
Prpty 1200000
Accident Psig 878
Mop Psig 936
Accident Pressure Pressure Did Not Exceed Mop
Pressure Restriction Ind No
Length Segment Isolated 16125
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 No
Cpm In Place Ind Yes
Cpm Operating Ind Yes
Cpm Functional Ind Yes
Cpm Detection Ind No
Cpm Conf Ind No
Investigation Status Yes, specify investigation result(s): (select all that apply)
Invest No Schedule Ind Yes
Invest No Schedule Ind Details The Investigation Did Not Reveal Any Fatigue Issues Since The Controller's Actions Were Deemed Appropriate For The Incident.
Invest No Control Room Ind Yes
Invest No Controller Ind Yes
Employee Drug Test Ind No
Contractor Drug Test Ind No
Cause Material Failure Of Pipe Or Weld
Cause Details Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Metallurgical Ind Yes
Failure Type Original Manufacturing-Related (Not Girth Weld Or Other Welds Formed In The Field)
Fatigue Vibr Related Yes
Failure Subtype Mechanically-Induced Fatigue Prior To Installation (Such As During Transport Of Pipe)
Additional Crack Ind Yes
Collected Data Ind Yes
Axial Magnetic Flx Lkg Ind Yes
Geometry Deformation Ind Yes
Axial Recent Year 2013
Geometry Recent Year 2013
Has Hydrtst Conduc Before Ind No
Direct Asmnt Conducted No
Non Destructive Exam Ind No
Preparer Name R****** K*****
Preparer Title Regulatory Specialist
Preparer Email R*************@s****.com
Preparer Telephone 713 241 1064
Preparer Fax 713 241 8498
Prepared Date 2016-10-24 00:00:00
Authorizer Name D****** P****
Authorizer Telephone 713 241 2035
Authorizer Title Integrity Regulatory Srvc Manager
Authorizer Email D************@s****.com
Narrative During a set point increase of three pounds of discharge pressure at an intermediate pump station by the controller, the pipe section approx. 0.5 miles downstream ruptured. The controller immediately identified the release by the pump station increased flow rate and low suction shutdown of the pump station. The controller took immediate action to shutdown the entire pipeline and closing intermediate block valves. The controller then closed off the receiving location to reduce the release of crude oil. The controllers actions from the time of the low suction shutdown of the pump station unit to the shutdown of the pipeline system was two minutes. This is faster than the cpm system can identify a release. The controller then contacted the local & on call supervisors, the controller console supervisor to inform them of his actions. The local supervisor called out two personnel to begin looking for the release site. Timing was after dark with limited visibility. The personnel drove the area north of the pump station. The topography is rolling hills and pasture land with limited access. They did not see the release site where they were able to drive. The air patrol was called to be over the pump station and head north at first light. The air patrol identified the location at 07:05 hrs. Metallurgical examination report - "the pipe section ruptured at a preexisting fatigue crack. The fatigue crack initiated from small corrosion pits along the internal surface at the toe of the longitudinal seam weld. Evidence of interlinked inclusions were observed, along with a stepwise fracture morphology, suggesting that stress-oriented hydrogen inducted cracking (sohic) may have contributed to the failure." 10/24/16 updated manufacturer armco 1982 & sub-cause original manufacturing-related.

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