GTG incident on 2023-10-18 — TX

Operator
Energy Transfer Company
Cause
Corrosion Failure
Commodity
Natural Gas
Program
GTG
Damage and Injuries
0 fatalities 0 injuries
Property damage (nominal)
$998,000
Incident datetime
2023-10-18 00:00 UTC
Report number
Location
TX
Narrative
On september 19, 2023 at approximately 0800, the control center received a call from a third party about a potential leak on the 88885654 wt apollo 6008442-wa 12in (howe 12in), located 12 miles south southwest of pyote, texas. The controller notified operations and at approximately 0900 the pipeline was blocked and isolated by operations. Once onsite, operations confirmed the pipeline had ruptured. Approximately 5.5 mmcf of natural gas was released. At 0730 the waha gas plant had an outage thus causing the pipeline to pressure up. The cause of the rupture is still under investigation. The ruptured portion of the pipe was cut out and sent to the lab for analysis. A supplemental report will be submitted once the investigation is complete, and the results are in from the lab. October 23, 2023 at approximately 0300, the pipeline was put back into service. The conclusion of the lab report revealed that the corrosion was primarily caused by the presence of hydrogen sulfide (h2s). To prevent this from occurring in the future, coupons were installed on the pipeline, this pipeline will be put on a weekly pigging schedule and inhibitors will continue to be injected into the pipeline. An ili run will be budgeted for 2025.
Detailed record list
Report Received Date
2023-10-18 00:00:00
Iyear
2023
Report Number
20230096
Supplemental Number
38766
Report Type
Supplemental Final
Operator Id
Name
Energy Transfer Company
Operator Street Address
1300 Main Street
Operator City Name
Houston
Operator State Abbreviation
TX
Operator Postal Code
77002
Time Zone
Central
Daylight Savings Ind
Yes
Location Latitude
Location Longitude
Nrc Rpt Num
Additional Nrc Report Numbers
1379829
Commodity Released Type
Natural Gas
Unintentional Release
5500
Intentional Release
0
Accompanying Liquid
70
Fatality Ind
No
Fatal
0
Injury Ind
No
Injure
0
Status When Identified
Normal Operation, Includes Pauses During Maintenance
Shutdown Due Accident Ind
Yes
Communication State Fed Ind
No
Ignite Ind
No
Upstream Action Taken
Valve Closure
Downstream Action Taken
Valve Closure
Num Pub Evacuated
0
On Off Shore
Onshore
Onshore State Abbreviation
Tx
Onshore Postal Code
79777
Onshore City Name
Pyote
Onshore County Name
Ward
Designated Location
Not Applicable
Pipe Fac Name
88885654 Wt Apollo 6008442-Wa 12in
Segment Name
Howe 12in
Federal
No
Location Type
Pipeline Right-Of-Way
Incident Area Type
Underground
Incident Area Subtype
Under Soil
Depth Of Cover
60
Other Underground Facilities
Yes
Crossing
No
Pipe Facility Type
Intrastate
System Part Involved
Onshore Pipeline, Including Valve Sites
Item Involved
Pipe
Pipe Type
Pipe Body
Pipe Diameter
12
Puddle Weld Ind
No
Pipe Wall Thickness
0.281
Pipe Smys
35000
Pipe Specification
Unknown
Pipe Seam Type
Longitudinal Erw - Unknown Frequency
Pipe Manufacturer
Unknown
Pipe Coating Type
Coal Tar
Coating Applied Ind
Unknown
Installation Year
1974
Manufactured Year
Unknown
Material Involved
Carbon Steel
Release Type
Rupture
Rupture Orient
Longitudinal
Rupture Length
12
Rupture Width
180
Class Location Type
Class 1 Location
Could Be Hca
No
Pir Radius
257
Heat Damage Ind
No
Non Heat Damage Ind
No
Did Occur In Mca Ind
No
Est Cost Oper Paid
0
Est Cost Unintentional Release
14740
Est Cost Intentional Release
0
Est Cost Prop Damage
998000
Est Cost Emergency
2000
Est Cost Other
0
Gas Cost In Mcf
2.68
Prpty
1014740
Num Persons Hosp Not Ovnght
0
Num Injured Treated By Emt
0
Num Resident Building Affctd
0
Num Business Building Affctd
0
Wildlife Impact Ind
No
Accident Psig
1048
Gas Flow In Pipe In Mcf
22.5
Mop Psig
1100
Mop Cfr Section
192.619(A)(1)
Maop Established Date
1974-01-01 00:00:00
Maop Reversal Flow Ind
No
Accident Pressure
Pressure Did Not Exceed Maop
Pressure Restriction Ind
No
Gas Required Odorized Ind
No
Upstream Valve Type Ind
Manual
Downstream Valve Type Ind
Manual
Length Segment Isolated
42179
Internal Inspection Ind
No
Other Inspection Ind
Yes
Internal Inspection Details
Needing Upgrade Launcher And Receivers
Operation Complications Ind
Yes
Other Complications Ind
Yes
Inspect Comp Details
Needing Upgrade Launcher And Receivers
Pipeline Function
Type C Gathering
Scada In Place Ind
Yes
Scada Operating Ind
Yes
Scada Functional Ind
Yes
Scada Detection Ind
No
Scada Conf Ind
No
Accident Identifier
Controller
Operator Type
Operator Employee
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
A review of the accident determined that there were no control room actions that contributed to the event
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
General Corrosion
Int Microbiological Ind
Yes
Int Metallurgical Basis Ind
Yes
Int Other Loc Ind
Yes
Corrosion Location Details
Top Quarter Of Pipe
Corrosion Inhibitors
Yes
Corrosion Lining
No
Cleaning Dewatering
Yes
Corrosion Coupons
No
Collected Data Ind
No
Has Hydrtst Conduc Before Ind
No
Direct Asmnt Conducted
No
Non Destructive Exam Ind
No
Preparer Name
C********** P******
Preparer Title
Sr. Specialist Dot Compliance
Preparer Email
C******************@e*************.com
Preparer Telephone
325-933-3577
Authorizer Name
S**** S*****
Authorizer Title
Director - Dot Compliance
Authorizer Telephone
405-557-5271
Authorizer Email
S***********@e*************.com
Narrative
On september 19, 2023 at approximately 0800, the control center received a call from a third party about a potential leak on the 88885654 wt apollo 6008442-wa 12in (howe 12in), located 12 miles south southwest of pyote, texas. The controller notified operations and at approximately 0900 the pipeline was blocked and isolated by operations. Once onsite, operations confirmed the pipeline had ruptured. Approximately 5.5 mmcf of natural gas was released. At 0730 the waha gas plant had an outage thus causing the pipeline to pressure up. The cause of the rupture is still under investigation. The ruptured portion of the pipe was cut out and sent to the lab for analysis. A supplemental report will be submitted once the investigation is complete, and the results are in from the lab. October 23, 2023 at approximately 0300, the pipeline was put back into service. The conclusion of the lab report revealed that the corrosion was primarily caused by the presence of hydrogen sulfide (h2s). To prevent this from occurring in the future, coupons were installed on the pipeline, this pipeline will be put on a weekly pigging schedule and inhibitors will continue to be injected into the pipeline. An ili run will be budgeted for 2025.
Report Received Date 2023-10-18 00:00:00
Iyear 2023
Report Number 20230096
Supplemental Number 38766
Report Type Supplemental Final
Operator Id 32099 PHMSA Enforcement
Name Energy Transfer Company
Operator Street Address 1300 Main Street
Operator City Name Houston
Operator State Abbreviation TX
Operator Postal Code 77002
Time Zone Central
Daylight Savings Ind Yes
Location Latitude 31.389161 Google Maps OpenStreetMap
Location Longitude -102.999949 Google Maps OpenStreetMap
Nrc Rpt Num 1379671 NRC Report How to search
Additional Nrc Report Numbers 1379829
Commodity Released Type Natural Gas
Unintentional Release 5500
Intentional Release 0
Accompanying Liquid 70
Fatality Ind No
Fatal 0
Injury Ind No
Injure 0
Status When Identified Normal Operation, Includes Pauses During Maintenance
Shutdown Due Accident Ind Yes
Communication State Fed Ind No
Ignite Ind No
Upstream Action Taken Valve Closure
Downstream Action Taken Valve Closure
Num Pub Evacuated 0
On Off Shore Onshore
Onshore State Abbreviation Tx
Onshore Postal Code 79777
Onshore City Name Pyote
Onshore County Name Ward
Designated Location Not Applicable
Pipe Fac Name 88885654 Wt Apollo 6008442-Wa 12in
Segment Name Howe 12in
Federal No
Location Type Pipeline Right-Of-Way
Incident Area Type Underground
Incident Area Subtype Under Soil
Depth Of Cover 60
Other Underground Facilities Yes
Crossing No
Pipe Facility Type Intrastate
System Part Involved Onshore Pipeline, Including Valve Sites
Item Involved Pipe
Pipe Type Pipe Body
Pipe Diameter 12
Puddle Weld Ind No
Pipe Wall Thickness 0.281
Pipe Smys 35000
Pipe Specification Unknown
Pipe Seam Type Longitudinal Erw - Unknown Frequency
Pipe Manufacturer Unknown
Pipe Coating Type Coal Tar
Coating Applied Ind Unknown
Installation Year 1974
Manufactured Year Unknown
Material Involved Carbon Steel
Release Type Rupture
Rupture Orient Longitudinal
Rupture Length 12
Rupture Width 180
Class Location Type Class 1 Location
Could Be Hca No
Pir Radius 257
Heat Damage Ind No
Non Heat Damage Ind No
Did Occur In Mca Ind No
Est Cost Oper Paid 0
Est Cost Unintentional Release 14740
Est Cost Intentional Release 0
Est Cost Prop Damage 998000
Est Cost Emergency 2000
Est Cost Other 0
Gas Cost In Mcf 2.68
Prpty 1014740
Num Persons Hosp Not Ovnght 0
Num Injured Treated By Emt 0
Num Resident Building Affctd 0
Num Business Building Affctd 0
Wildlife Impact Ind No
Accident Psig 1048
Gas Flow In Pipe In Mcf 22.5
Mop Psig 1100
Mop Cfr Section 192.619(A)(1) View CFR 49 §192
Maop Established Date 1974-01-01 00:00:00
Maop Reversal Flow Ind No
Accident Pressure Pressure Did Not Exceed Maop
Pressure Restriction Ind No
Gas Required Odorized Ind No
Upstream Valve Type Ind Manual
Downstream Valve Type Ind Manual
Length Segment Isolated 42179
Internal Inspection Ind No
Other Inspection Ind Yes
Internal Inspection Details Needing Upgrade Launcher And Receivers
Operation Complications Ind Yes
Other Complications Ind Yes
Inspect Comp Details Needing Upgrade Launcher And Receivers
Pipeline Function Type C Gathering
Scada In Place Ind Yes
Scada Operating Ind Yes
Scada Functional Ind Yes
Scada Detection Ind No
Scada Conf Ind No
Accident Identifier Controller
Operator Type Operator Employee
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 A review of the accident determined that there were no control room actions that contributed to the event
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 General Corrosion
Int Microbiological Ind Yes
Int Metallurgical Basis Ind Yes
Int Other Loc Ind Yes
Corrosion Location Details Top Quarter Of Pipe
Corrosion Inhibitors Yes
Corrosion Lining No
Cleaning Dewatering Yes
Corrosion Coupons No
Collected Data Ind No
Has Hydrtst Conduc Before Ind No
Direct Asmnt Conducted No
Non Destructive Exam Ind No
Preparer Name C********** P******
Preparer Title Sr. Specialist Dot Compliance
Preparer Email C******************@e*************.com
Preparer Telephone 325-933-3577
Authorizer Name S**** S*****
Authorizer Title Director - Dot Compliance
Authorizer Telephone 405-557-5271
Authorizer Email S***********@e*************.com
Narrative On september 19, 2023 at approximately 0800, the control center received a call from a third party about a potential leak on the 88885654 wt apollo 6008442-wa 12in (howe 12in), located 12 miles south southwest of pyote, texas. The controller notified operations and at approximately 0900 the pipeline was blocked and isolated by operations. Once onsite, operations confirmed the pipeline had ruptured. Approximately 5.5 mmcf of natural gas was released. At 0730 the waha gas plant had an outage thus causing the pipeline to pressure up. The cause of the rupture is still under investigation. The ruptured portion of the pipe was cut out and sent to the lab for analysis. A supplemental report will be submitted once the investigation is complete, and the results are in from the lab. October 23, 2023 at approximately 0300, the pipeline was put back into service. The conclusion of the lab report revealed that the corrosion was primarily caused by the presence of hydrogen sulfide (h2s). To prevent this from occurring in the future, coupons were installed on the pipeline, this pipeline will be put on a weekly pigging schedule and inhibitors will continue to be injected into the pipeline. An ili run will be budgeted for 2025.

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