HL incident on 2018-10-11 — TX

Operator
Phillips 66 Pipeline Llc
Cause
Incorrect Operation
Commodity
Hvl Or Other Flammable Or Toxic Fluid Which Is A Gas At Ambient Conditions
Program
HL
Damage and Injuries
0 fatalities 0 injuries
Property damage (nominal)
$65,000
Incident datetime
2018-10-11 11:10
Report number
Location
TX
Narrative
On october 11, 2018, an anomaly repair crew was in the process of installing a full wrap sleeve on mx-20 (at eng station 476+77) as a repair for an internal metal loss ili tool run feature. At approximately 11:10 am, a weld burn through occurred during in-service welding (at ~6 oclock position) while in the process of installing the first butter pass/temper bead on a circumferential weld for the sleeve. A small fire ensued that was immediately extinguished by the two fire-watches on site. No injuries occurred and the line was immediately shut down, isolated and efforts initiated to reduce pressure on the pipeline segment. The pipeline segment was isolated and purged and the affected area of pipe was removed and replaced with new pipe. The pipeline was then returned to service at 8:00 am on monday, october 15, 2018. The primary cause of this incident is related to a thin wall internal corrosion area on the bottom of the pipe at the location of the sleeve circumferential weld that was not identified during the ut testing of the area prior to welding. The pipe wall thickness in this area was too thin to support in-service welding and so the weld penetrated the pipe wall. An epoch 650 dual element probe was used to perform the pipe wall thickness testing prior to welding of the circumferential welds for the sleeve. With this type of ut instrument, and under certain circumstances of pipe wall thickness and corrosion geometry, it is possible to get a false indication of pipe wall thickness that is a multiple of the actual remaining wall thickness. In this case, the ndt technician received a false thickness ut reading which was believed to be adequate for in-service welding. P66 is currently evaluating improvements to ut procedures and processes to reduce the likelihood of getting false thickness indications in similar situations. Based on these evaluations, appropriate changes to ut procedures will be implemented. This report was updated / modified per comments received from PHMSA accident investigation division and is submitted as a final report.
Detailed record list
Report Received Date
2018-11-08 00:00:00
Iyear
2018
Report Number
20180343
Supplemental Number
31209
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
2018-10-11 11:10:00
Location Latitude
Location Longitude
Commodity Released Type
Hvl Or Other Flammable Or Toxic Fluid Which Is A Gas At Ambient Conditions
Commodity Subtype
Lpg (Liquefied Petroleum Gas) / Ngl (Natural Gas Liquid)
Unintentional Release Bbls
0.07
Intentional Release Bbls
1200
Recovered Bbls
0
Fatality Ind
No
Fatal
0
Injury Ind
No
Injure
0
Accident Identifier
Local Operating Personnel, Including Contractors
Operator Type
Contractor Working For The Operator
Incident Identified Datetime
2018-10-11 11:10:00
System Part Involved
Onshore Pipeline, Including Valve Sites
On Off Shore
Onshore
Shutdown Due Accident Ind
Yes
Shutdown Datetime
2018-10-11 11:15:00
Restart Datetime
2018-10-15 08:00:00
On Site Datetime
2018-10-11 11:10:00
Nrc Rpt Datetime
2018-10-11 12:06:00
Nrc Rpt Num
Ignite Ind
Yes
Explode Ind
No
Upstream Valve Type Ind
Manual
Downstream Valve Type Ind
Manual
Num Pub Evacuated
0
Pipe Fac Name
Mx-20
Segment Name
Gaines To Goldsmith
Onshore State Abbreviation
Tx
Onshore Postal Code
79714
Onshore City Name
Not Within A Municipality
Onshore County Name
Andrews
Designated Location
Survey Station No.
Designated Name
476+77
Federal
No
Location Type
Pipeline Right-Of-Way
Incident Area Type
Underground
Incident Area Subtype
Exposed Due To Excavation
Depth Of Cover
18
Crossing
No
Pipe Facility Type
Interstate
Item Involved
Pipe
Pipe Type
Pipe Body
Pipe Diameter
8
Pipe Wall Thickness
0.188
Pipe Smys
45000
Pipe Specification
Api-5l
Pipe Seam Type
Erw - Low Frequency
Pipe Manufacturer
Unknown
Pipe Coating Type
Coal Tar
Weld Subtype
Other
Installation Year
1944
Manufactured Year
Unknown
Material Involved
Carbon Steel
Release Type
Leak
Leak Type
Pinhole
Leak Type Other
Weld Blow Through Pinhole
Rupture Details
Located At The 6 O'clock Position
Wildlife Impact Ind
No
Soil Contamination
No
Long Term Assessment
No
Remediation Ind
No
Water Contam Ind
No
Could Be Hca
No
Commodity Reached Hca
No
Est Cost Oper Paid
0
Est Cost Gas Released
84000
Est Cost Prop Damage
65000
Est Cost Emergency
0
Est Cost Environmental
0
Est Cost Other
0
Prpty
149000
Accident Psig
650
Mop Psig
1005
Accident Pressure
Pressure Did Not Exceed Mop
Pressure Restriction Ind
No
Length Segment Isolated
42240
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
No
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
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
Leak caused by weld blow through on the line. Controller actions could not have contributed to the incident
Employee Drug Test Ind
No
Contractor Drug Test Ind
Yes
Num Contractors Tested
2
Num Contractors Failed
0
Cause
Incorrect Operation
Cause Details
Other Incorrect Operation
Operation Type
Other Incorrect Operation
Operation Details
Accidental Ignition During Maintenance Welding Operation
Related Other Ind
Yes
Operation Related Details
Inadequate Ut Thickness Testing
Category Type
Routine Maintenance
Operator Qualification Ind
Yes
Qualified Individuals
Yes, They Were Qualified For The Task(S)
Preparer Name
C**** F*****
Preparer Title
Dot Coordinator
Preparer Email
C*************@p**.com
Preparer Telephone
303-862-1189
Prepared Date
2018-11-20 00:00:00
Authorizer Name
T*** F****
Authorizer Telephone
8327651632
Authorizer Title
Director Dot Compliance
Authorizer Email
M***********@p**.com
Narrative
On october 11, 2018, an anomaly repair crew was in the process of installing a full wrap sleeve on mx-20 (at eng station 476+77) as a repair for an internal metal loss ili tool run feature. At approximately 11:10 am, a weld burn through occurred during in-service welding (at ~6 oclock position) while in the process of installing the first butter pass/temper bead on a circumferential weld for the sleeve. A small fire ensued that was immediately extinguished by the two fire-watches on site. No injuries occurred and the line was immediately shut down, isolated and efforts initiated to reduce pressure on the pipeline segment. The pipeline segment was isolated and purged and the affected area of pipe was removed and replaced with new pipe. The pipeline was then returned to service at 8:00 am on monday, october 15, 2018. The primary cause of this incident is related to a thin wall internal corrosion area on the bottom of the pipe at the location of the sleeve circumferential weld that was not identified during the ut testing of the area prior to welding. The pipe wall thickness in this area was too thin to support in-service welding and so the weld penetrated the pipe wall. An epoch 650 dual element probe was used to perform the pipe wall thickness testing prior to welding of the circumferential welds for the sleeve. With this type of ut instrument, and under certain circumstances of pipe wall thickness and corrosion geometry, it is possible to get a false indication of pipe wall thickness that is a multiple of the actual remaining wall thickness. In this case, the ndt technician received a false thickness ut reading which was believed to be adequate for in-service welding. P66 is currently evaluating improvements to ut procedures and processes to reduce the likelihood of getting false thickness indications in similar situations. Based on these evaluations, appropriate changes to ut procedures will be implemented. This report was updated / modified per comments received from PHMSA accident investigation division and is submitted as a final report.
Report Received Date 2018-11-08 00:00:00
Iyear 2018
Report Number 20180343
Supplemental Number 31209
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 2018-10-11 11:10:00
Location Latitude 32.1014 Google Maps OpenStreetMap
Location Longitude -102.70702 Google Maps OpenStreetMap
Commodity Released Type Hvl Or Other Flammable Or Toxic Fluid Which Is A Gas At Ambient Conditions
Commodity Subtype Lpg (Liquefied Petroleum Gas) / Ngl (Natural Gas Liquid)
Unintentional Release Bbls 0.07
Intentional Release Bbls 1200
Recovered Bbls 0
Fatality Ind No
Fatal 0
Injury Ind No
Injure 0
Accident Identifier Local Operating Personnel, Including Contractors
Operator Type Contractor Working For The Operator
Incident Identified Datetime 2018-10-11 11:10:00
System Part Involved Onshore Pipeline, Including Valve Sites
On Off Shore Onshore
Shutdown Due Accident Ind Yes
Shutdown Datetime 2018-10-11 11:15:00
Restart Datetime 2018-10-15 08:00:00
On Site Datetime 2018-10-11 11:10:00
Nrc Rpt Datetime 2018-10-11 12:06:00
Nrc Rpt Num 1227211 NRC Report How to search
Ignite Ind Yes
Explode Ind No
Upstream Valve Type Ind Manual
Downstream Valve Type Ind Manual
Num Pub Evacuated 0
Pipe Fac Name Mx-20
Segment Name Gaines To Goldsmith
Onshore State Abbreviation Tx
Onshore Postal Code 79714
Onshore City Name Not Within A Municipality
Onshore County Name Andrews
Designated Location Survey Station No.
Designated Name 476+77
Federal No
Location Type Pipeline Right-Of-Way
Incident Area Type Underground
Incident Area Subtype Exposed Due To Excavation
Depth Of Cover 18
Crossing No
Pipe Facility Type Interstate
Item Involved Pipe
Pipe Type Pipe Body
Pipe Diameter 8
Pipe Wall Thickness 0.188
Pipe Smys 45000
Pipe Specification Api-5l
Pipe Seam Type Erw - Low Frequency
Pipe Manufacturer Unknown
Pipe Coating Type Coal Tar
Weld Subtype Other
Installation Year 1944
Manufactured Year Unknown
Material Involved Carbon Steel
Release Type Leak
Leak Type Pinhole
Leak Type Other Weld Blow Through Pinhole
Rupture Details Located At The 6 O'clock Position
Wildlife Impact Ind No
Soil Contamination No
Long Term Assessment No
Remediation Ind No
Water Contam Ind No
Could Be Hca No
Commodity Reached Hca No
Est Cost Oper Paid 0
Est Cost Gas Released 84000
Est Cost Prop Damage 65000
Est Cost Emergency 0
Est Cost Environmental 0
Est Cost Other 0
Prpty 149000
Accident Psig 650
Mop Psig 1005
Accident Pressure Pressure Did Not Exceed Mop
Pressure Restriction Ind No
Length Segment Isolated 42240
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 No
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 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 Leak caused by weld blow through on the line. Controller actions could not have contributed to the incident
Employee Drug Test Ind No
Contractor Drug Test Ind Yes
Num Contractors Tested 2
Num Contractors Failed 0
Cause Incorrect Operation
Cause Details Other Incorrect Operation
Operation Type Other Incorrect Operation
Operation Details Accidental Ignition During Maintenance Welding Operation
Related Other Ind Yes
Operation Related Details Inadequate Ut Thickness Testing
Category Type Routine Maintenance
Operator Qualification Ind Yes
Qualified Individuals Yes, They Were Qualified For The Task(S)
Preparer Name C**** F*****
Preparer Title Dot Coordinator
Preparer Email C*************@p**.com
Preparer Telephone 303-862-1189
Prepared Date 2018-11-20 00:00:00
Authorizer Name T*** F****
Authorizer Telephone 8327651632
Authorizer Title Director Dot Compliance
Authorizer Email M***********@p**.com
Narrative On october 11, 2018, an anomaly repair crew was in the process of installing a full wrap sleeve on mx-20 (at eng station 476+77) as a repair for an internal metal loss ili tool run feature. At approximately 11:10 am, a weld burn through occurred during in-service welding (at ~6 oclock position) while in the process of installing the first butter pass/temper bead on a circumferential weld for the sleeve. A small fire ensued that was immediately extinguished by the two fire-watches on site. No injuries occurred and the line was immediately shut down, isolated and efforts initiated to reduce pressure on the pipeline segment. The pipeline segment was isolated and purged and the affected area of pipe was removed and replaced with new pipe. The pipeline was then returned to service at 8:00 am on monday, october 15, 2018. The primary cause of this incident is related to a thin wall internal corrosion area on the bottom of the pipe at the location of the sleeve circumferential weld that was not identified during the ut testing of the area prior to welding. The pipe wall thickness in this area was too thin to support in-service welding and so the weld penetrated the pipe wall. An epoch 650 dual element probe was used to perform the pipe wall thickness testing prior to welding of the circumferential welds for the sleeve. With this type of ut instrument, and under certain circumstances of pipe wall thickness and corrosion geometry, it is possible to get a false indication of pipe wall thickness that is a multiple of the actual remaining wall thickness. In this case, the ndt technician received a false thickness ut reading which was believed to be adequate for in-service welding. P66 is currently evaluating improvements to ut procedures and processes to reduce the likelihood of getting false thickness indications in similar situations. Based on these evaluations, appropriate changes to ut procedures will be implemented. This report was updated / modified per comments received from PHMSA accident investigation division and is submitted as a final report.

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