HL incident on 2014-10-06 — TX

Operator
Phillips 66 Pipeline Llc
Cause
Corrosion Failure
Commodity
Crude Oil
Program
HL
Damage and Injuries
0 fatalities 0 injuries
Property damage (nominal)
$10,000
Incident datetime
2014-10-06 01:43
Report number
Location
TX
Narrative
This failure occurred on the tank manifold piping at the odessa crude terminal and did not affect mainline pipeline operations. The failure mechanism was internal corrosion. The mop in this section of pipe is 285 psig and the line was not overpressured prior to the failure. The section of pipe which failed was isolated, drained and a clamp was installed. To prevent further leakage and excess spill crude recovered via a vacuum truck. To prevent internal corrosion on this line segment in the future, a new section of pipe has been constructed, hydrotested and internally coated. The new pipe segment will be installed by december 1. Update - 12/30/2014 - the section of pipe which corroded and leak has been replaced with a new section of pipe which has been internally coated to prevent internal corrosion (which was the corrosion mechanism of this failure). Update - 5/4/2015 - this is submittal of a supplemental report at the request of jocelyn kerl so as to change the report to the long form which requires more information. No previous submitted information was changed, only new information added per the requirements of the long form.
Detailed record list
Report Received Date
2014-11-05 00:00:00
Iyear
2014
Report Number
20140389
Supplemental Number
20404
Report Type
Supplemental Final
Operator Id
Name
Phillips 66 Pipeline Llc
Operator Street Address
2331 Citywest Blvd
Operator City Name
Houston
Operator State Abbreviation
TX
Operator Postal Code
77042
Local Datetime
2014-10-06 01:43:00
Location Latitude
Location Longitude
Commodity Released Type
Crude Oil
Unintentional Release Bbls
0.44
Recovered Bbls
0.25
Fatality Ind
No
Fatal
0
Injury Ind
No
Injure
0
Accident Identifier
Local Operating Personnel, Including Contractors
Operator Type
Operator Employee
Incident Identified Datetime
2014-10-06 01:43:00
System Part Involved
Onshore Terminal/tank Farm Equipment And Piping
On Off Shore
Onshore
Shutdown Due Accident Ind
No
Shutdown Explain
Leak In Terminal Pipe Manifold. Line Isolated, Pipelines Continue To Operate
On Site Datetime
2014-10-06 01:43:00
Nrc Rpt Num
Nrc Notification Not Required
Ignite Ind
No
Explode Ind
No
Num Pub Evacuated
0
Pipe Fac Name
Odessa Crude Terminal
Segment Name
Manifold
Onshore State Abbreviation
Tx
Onshore Postal Code
79741
Onshore City Name
Goldsmith
Onshore County Name
Ector
Designated Location
Milepost/valve Station
Designated Name
Station
Federal
No
Location Type
Totally Contained On Operator-Controlled Property
Incident Area Type
Aboveground
Incident Area Subtype
Typical Aboveground Facility Piping Or Appurtenance
Crossing
No
Pipe Facility Type
Interstate
Item Involved
Pipe
Pipe Type
Pipe Body
Pipe Diameter
16
Pipe Wall Thickness
0.25
Pipe Smys
42000
Pipe Specification
Api-5l X-42
Pipe Seam Type
Seamless
Pipe Manufacturer
Unknown
Pipe Coating Type
Paint
Installation Year
Unknown
Manufactured Year
Unknown
Material Involved
Carbon Steel
Release Type
Leak
Leak Type
Pinhole
Wildlife Impact Ind
No
Soil Contamination
Yes
Long Term Assessment
No
Remediation Ind
Yes
Soil Remed Ind
Yes
Water Contam Ind
No
Could Be Hca
No
Commodity Reached Hca
No
Est Cost Oper Paid
0
Est Cost Gas Released
50
Est Cost Prop Damage
10000
Est Cost Emergency
0
Est Cost Environmental
5000
Est Cost Other
0
Prpty
15050
Accident Psig
65
Mop Psig
275
Accident Pressure
Pressure Did Not Exceed Mop
Pressure Restriction Ind
No
Pipeline Function
< 20% Smys Regulated Transmission
Scada In Place Ind
Yes
Scada Operating Ind
Yes
Scada Functional Ind
Yes
Scada Detection Ind
No
Scada Conf Ind
No
Cpm In Place Ind
No
Investigation Status
No, the operator did not find that an investigation of the controller(s) actions or control room issues was necessary due to: (provide an explanation for why the operator did not investigate)
Investigation Status Details
This was an internal corrosion issue, so controller actions could not have contributed to the incident
Employee Drug Test Ind
No
Contractor Drug Test Ind
No
Cause
Corrosion Failure
Cause Details
Internal Corrosion
Internal External
Internal Corrosion
Int Visual Exam Results
Localized Pitting
Int Microbiological Ind
Yes
Int Field Exam Basis Ind
Yes
Int Metallurgical Basis Ind
Yes
Int Low Point Pipe Loc Ind
Yes
Corrosion Inhibitors
Yes
Corrosion Lining
No
Cleaning Dewatering
Not Applicable - Not Mainline Pipe
Corrosion Coupons
Not Applicable - Not Mainline Pipe
Collected Data Ind
No
Has Hydrtst Conduc Before Ind
No
Direct Asmnt Conducted
No
Non Destructive Exam Ind
No
Preparer Name
C**** F*****
Preparer Title
Dot Coordinator
Preparer Email
C*************@p**.com
Preparer Telephone
303-862-1189
Preparer Fax
918-977-8545
Prepared Date
2015-05-04 00:00:00
Authorizer Name
T*** T*****
Authorizer Telephone
832-765-1636
Authorizer Title
Mgr. Regulatory Compliance
Authorizer Email
T************@p**.com
Narrative
This failure occurred on the tank manifold piping at the odessa crude terminal and did not affect mainline pipeline operations. The failure mechanism was internal corrosion. The mop in this section of pipe is 285 psig and the line was not overpressured prior to the failure. The section of pipe which failed was isolated, drained and a clamp was installed. To prevent further leakage and excess spill crude recovered via a vacuum truck. To prevent internal corrosion on this line segment in the future, a new section of pipe has been constructed, hydrotested and internally coated. The new pipe segment will be installed by december 1. Update - 12/30/2014 - the section of pipe which corroded and leak has been replaced with a new section of pipe which has been internally coated to prevent internal corrosion (which was the corrosion mechanism of this failure). Update - 5/4/2015 - this is submittal of a supplemental report at the request of jocelyn kerl so as to change the report to the long form which requires more information. No previous submitted information was changed, only new information added per the requirements of the long form.
Report Received Date 2014-11-05 00:00:00
Iyear 2014
Report Number 20140389
Supplemental Number 20404
Report Type Supplemental Final
Operator Id 31684 PHMSA Enforcement
Name Phillips 66 Pipeline Llc
Operator Street Address 2331 Citywest Blvd
Operator City Name Houston
Operator State Abbreviation TX
Operator Postal Code 77042
Local Datetime 2014-10-06 01:43:00
Location Latitude 31.950527 Google Maps OpenStreetMap
Location Longitude -102.603994 Google Maps OpenStreetMap
Commodity Released Type Crude Oil
Unintentional Release Bbls 0.44
Recovered Bbls 0.25
Fatality Ind No
Fatal 0
Injury Ind No
Injure 0
Accident Identifier Local Operating Personnel, Including Contractors
Operator Type Operator Employee
Incident Identified Datetime 2014-10-06 01:43:00
System Part Involved Onshore Terminal/tank Farm Equipment And Piping
On Off Shore Onshore
Shutdown Due Accident Ind No
Shutdown Explain Leak In Terminal Pipe Manifold. Line Isolated, Pipelines Continue To Operate
On Site Datetime 2014-10-06 01:43:00
Nrc Rpt Num Nrc Notification Not Required NRC Report How to search
Ignite Ind No
Explode Ind No
Num Pub Evacuated 0
Pipe Fac Name Odessa Crude Terminal
Segment Name Manifold
Onshore State Abbreviation Tx
Onshore Postal Code 79741
Onshore City Name Goldsmith
Onshore County Name Ector
Designated Location Milepost/valve Station
Designated Name Station
Federal No
Location Type Totally Contained On Operator-Controlled Property
Incident Area Type Aboveground
Incident Area Subtype Typical Aboveground Facility Piping Or Appurtenance
Crossing No
Pipe Facility Type Interstate
Item Involved Pipe
Pipe Type Pipe Body
Pipe Diameter 16
Pipe Wall Thickness 0.25
Pipe Smys 42000
Pipe Specification Api-5l X-42
Pipe Seam Type Seamless
Pipe Manufacturer Unknown
Pipe Coating Type Paint
Installation Year Unknown
Manufactured Year Unknown
Material Involved Carbon Steel
Release Type Leak
Leak Type Pinhole
Wildlife Impact Ind No
Soil Contamination Yes
Long Term Assessment No
Remediation Ind Yes
Soil Remed Ind Yes
Water Contam Ind No
Could Be Hca No
Commodity Reached Hca No
Est Cost Oper Paid 0
Est Cost Gas Released 50
Est Cost Prop Damage 10000
Est Cost Emergency 0
Est Cost Environmental 5000
Est Cost Other 0
Prpty 15050
Accident Psig 65
Mop Psig 275
Accident Pressure Pressure Did Not Exceed Mop
Pressure Restriction Ind No
Pipeline Function < 20% Smys Regulated Transmission
Scada In Place Ind Yes
Scada Operating Ind Yes
Scada Functional Ind Yes
Scada Detection Ind No
Scada Conf Ind No
Cpm In Place Ind No
Investigation Status No, the operator did not find that an investigation of the controller(s) actions or control room issues was necessary due to: (provide an explanation for why the operator did not investigate)
Investigation Status Details This was an internal corrosion issue, so controller actions could not have contributed to the incident
Employee Drug Test Ind No
Contractor Drug Test Ind No
Cause Corrosion Failure
Cause Details Internal Corrosion
Internal External Internal Corrosion
Int Visual Exam Results Localized Pitting
Int Microbiological Ind Yes
Int Field Exam Basis Ind Yes
Int Metallurgical Basis Ind Yes
Int Low Point Pipe Loc Ind Yes
Corrosion Inhibitors Yes
Corrosion Lining No
Cleaning Dewatering Not Applicable - Not Mainline Pipe
Corrosion Coupons Not Applicable - Not Mainline Pipe
Collected Data Ind No
Has Hydrtst Conduc Before Ind No
Direct Asmnt Conducted No
Non Destructive Exam Ind No
Preparer Name C**** F*****
Preparer Title Dot Coordinator
Preparer Email C*************@p**.com
Preparer Telephone 303-862-1189
Preparer Fax 918-977-8545
Prepared Date 2015-05-04 00:00:00
Authorizer Name T*** T*****
Authorizer Telephone 832-765-1636
Authorizer Title Mgr. Regulatory Compliance
Authorizer Email T************@p**.com
Narrative This failure occurred on the tank manifold piping at the odessa crude terminal and did not affect mainline pipeline operations. The failure mechanism was internal corrosion. The mop in this section of pipe is 285 psig and the line was not overpressured prior to the failure. The section of pipe which failed was isolated, drained and a clamp was installed. To prevent further leakage and excess spill crude recovered via a vacuum truck. To prevent internal corrosion on this line segment in the future, a new section of pipe has been constructed, hydrotested and internally coated. The new pipe segment will be installed by december 1. Update - 12/30/2014 - the section of pipe which corroded and leak has been replaced with a new section of pipe which has been internally coated to prevent internal corrosion (which was the corrosion mechanism of this failure). Update - 5/4/2015 - this is submittal of a supplemental report at the request of jocelyn kerl so as to change the report to the long form which requires more information. No previous submitted information was changed, only new information added per the requirements of the long form.

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