HL incident on 2015-06-01 — KS

Operator
Nustar Pipeline Operating Partnership L.p.
Cause
Material Failure Of Pipe Or Weld
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)
$49,400
Incident datetime
2015-06-01 02:28
Report number
Location
KS
Narrative
At 2:28 am on 06-01-2015 the san antonio control center received an ammonia detection alarm and station lockout at the ramah pump station, in iberville parrish, la. A station lockout isolates the station piping from the mainline piping. The control center operator contacted the area nustar employee. The nustar employee arrived at 4:09 am and confirmed the smell of ammonia originating from buried mainline pipe within the pump station and not the station piping. Emergency shutdown procedures for the mainline were started at 0412. The pipeline was completely shut down and blocked at 0421. Nustar's maintenance crew arrived on 06-02-2015, excavated and installed a stopple tee downstream of the leak location. On 06-03-2015 they excavated the pipeline and confirmed the stopple tee fitting as the cause. They completed repairs on 06-03-2015 and the line was restarted at 23:45. The stopple tee fitting will be sent for metallurgical analysis in order to determine the cause of the leak. Results of metallurgical analysis: the leak was caused by a nearly through wall crack in the longitudinal seam weld of the stopple(r) fitting. The crack initiated in an area of misalignment of the cuff edges and incomplete penetration (ip); these are fabrication defects created during installation of the fitting. The ip created a notch-like stress concentration which allowed for the initiation of a crack. The crack propagated until it was nearly through the weld. The remaining intact ligament was unable to contain the internal line pressure.
Detailed record list
Report Received Date
2015-06-30 00:00:00
Iyear
2015
Report Number
20150237
Supplemental Number
21807
Report Type
Supplemental Final
Operator Id
Name
Nustar Pipeline Operating Partnership L.p.
Operator Street Address
7340 W. 21st Street N., Suite 200
Operator City Name
Wichita
Operator State Abbreviation
KS
Operator Postal Code
67205
Local Datetime
2015-06-01 04:09:00
Location Latitude
Location Longitude
Commodity Released Type
Hvl Or Other Flammable Or Toxic Fluid Which Is A Gas At Ambient Conditions
Commodity Subtype
Anhydrous Ammonia
Unintentional Release Bbls
8.98
Intentional Release Bbls
9.63
Recovered Bbls
7.18
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
2015-06-01 02:28:00
System Part Involved
Onshore Pipeline, Including Valve Sites
On Off Shore
Onshore
Shutdown Due Accident Ind
Yes
Shutdown Datetime
2015-06-01 02:28:00
Restart Datetime
2015-06-03 23:45:00
On Site Datetime
2015-06-01 04:09:00
Nrc Rpt Datetime
2015-06-01 10:22:00
Nrc Rpt Num
Ignite Ind
No
Explode Ind
No
Upstream Valve Type Ind
Remotely Controlled
Downstream Valve Type Ind
Manual
Num Pub Evacuated
0
Pipe Fac Name
Ramah Pump Station
Segment Name
Ramah 8 Inch To Palmetto Station
Onshore State Abbreviation
La
Onshore Postal Code
70757
Onshore City Name
Not Within A Municipality
Onshore County Name
Iberville
Designated Location
Survey Station No.
Designated Name
2495+35
Federal
No
Location Type
Totally Contained On Operator-Controlled Property
Incident Area Type
Underground
Incident Area Subtype
Under Soil
Depth Of Cover
48
Crossing
No
Pipe Facility Type
Interstate
Item Involved
Weld, Including Heat-Affected Zone
Weld Subtype
Other
Weld Details
Longitudinal
Installation Year
2003
Material Involved
Carbon Steel
Release Type
Leak
Leak Type
Crack
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
No
Est Cost Oper Paid
0
Est Cost Gas Released
635
Est Cost Prop Damage
49400
Est Cost Emergency
17820
Est Cost Environmental
0
Est Cost Other
0
Prpty
67855
Accident Psig
1320
Mop Psig
1340
Accident Pressure
Pressure Did Not Exceed Mop
Pressure Restriction Ind
No
Length Segment Isolated
47520
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
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
The operator's actions did not contribute to the cause of the accident.
Employee Drug Test Ind
No
Contractor Drug Test Ind
No
Cause
Material Failure Of Pipe Or Weld
Cause Details
Design-, Construction-, Installation-, Or Fabrication-Related
Metallurgical Ind
Yes
Failure Type
Design-, Construction-, Installation-, Or Fabrication-Related
Other Factor
Yes
Other Factor Details
Incomplete Penetration Created A Notch Like Stress Concentration Which Allowed F
Pwf Additional Other Ind
Yes
Collected Data Ind
Yes
Other Tool Tech Ind
Yes
Other Tool
Def&mfl Tool Runs 12/10/14, Def&mfl Tool Runs 10/19/11, Def&mfl Tool Runs 6/7/06
Other Recent Year
2014
Has Hydrtst Conduc Before Ind
No
Direct Asmnt Conducted
No
Non Destructive Exam Ind
No
Preparer Name
K*** P****
Preparer Title
Pipeline Safety Supervisor
Preparer Email
K*********@n***********.com
Preparer Telephone
316-721-7053
Prepared Date
2016-09-28 00:00:00
Authorizer Name
B*** F******
Authorizer Telephone
316-721-7066
Authorizer Title
General Manager - Pipeline And Terminal Operations
Authorizer Email
B***********@n***********.com
Narrative
At 2:28 am on 06-01-2015 the san antonio control center received an ammonia detection alarm and station lockout at the ramah pump station, in iberville parrish, la. A station lockout isolates the station piping from the mainline piping. The control center operator contacted the area nustar employee. The nustar employee arrived at 4:09 am and confirmed the smell of ammonia originating from buried mainline pipe within the pump station and not the station piping. Emergency shutdown procedures for the mainline were started at 0412. The pipeline was completely shut down and blocked at 0421. Nustar's maintenance crew arrived on 06-02-2015, excavated and installed a stopple tee downstream of the leak location. On 06-03-2015 they excavated the pipeline and confirmed the stopple tee fitting as the cause. They completed repairs on 06-03-2015 and the line was restarted at 23:45. The stopple tee fitting will be sent for metallurgical analysis in order to determine the cause of the leak. Results of metallurgical analysis: the leak was caused by a nearly through wall crack in the longitudinal seam weld of the stopple(r) fitting. The crack initiated in an area of misalignment of the cuff edges and incomplete penetration (ip); these are fabrication defects created during installation of the fitting. The ip created a notch-like stress concentration which allowed for the initiation of a crack. The crack propagated until it was nearly through the weld. The remaining intact ligament was unable to contain the internal line pressure.
Report Received Date 2015-06-30 00:00:00
Iyear 2015
Report Number 20150237
Supplemental Number 21807
Report Type Supplemental Final
Operator Id 10012 PHMSA Enforcement
Name Nustar Pipeline Operating Partnership L.p.
Operator Street Address 7340 W. 21st Street N., Suite 200
Operator City Name Wichita
Operator State Abbreviation KS
Operator Postal Code 67205
Local Datetime 2015-06-01 04:09:00
Location Latitude 30.386817 Google Maps OpenStreetMap
Location Longitude -91.507267 Google Maps OpenStreetMap
Commodity Released Type Hvl Or Other Flammable Or Toxic Fluid Which Is A Gas At Ambient Conditions
Commodity Subtype Anhydrous Ammonia
Unintentional Release Bbls 8.98
Intentional Release Bbls 9.63
Recovered Bbls 7.18
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 2015-06-01 02:28:00
System Part Involved Onshore Pipeline, Including Valve Sites
On Off Shore Onshore
Shutdown Due Accident Ind Yes
Shutdown Datetime 2015-06-01 02:28:00
Restart Datetime 2015-06-03 23:45:00
On Site Datetime 2015-06-01 04:09:00
Nrc Rpt Datetime 2015-06-01 10:22:00
Nrc Rpt Num 1120335 NRC Report How to search
Ignite Ind No
Explode Ind No
Upstream Valve Type Ind Remotely Controlled
Downstream Valve Type Ind Manual
Num Pub Evacuated 0
Pipe Fac Name Ramah Pump Station
Segment Name Ramah 8 Inch To Palmetto Station
Onshore State Abbreviation La
Onshore Postal Code 70757
Onshore City Name Not Within A Municipality
Onshore County Name Iberville
Designated Location Survey Station No.
Designated Name 2495+35
Federal No
Location Type Totally Contained On Operator-Controlled Property
Incident Area Type Underground
Incident Area Subtype Under Soil
Depth Of Cover 48
Crossing No
Pipe Facility Type Interstate
Item Involved Weld, Including Heat-Affected Zone
Weld Subtype Other
Weld Details Longitudinal
Installation Year 2003
Material Involved Carbon Steel
Release Type Leak
Leak Type Crack
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 No
Est Cost Oper Paid 0
Est Cost Gas Released 635
Est Cost Prop Damage 49400
Est Cost Emergency 17820
Est Cost Environmental 0
Est Cost Other 0
Prpty 67855
Accident Psig 1320
Mop Psig 1340
Accident Pressure Pressure Did Not Exceed Mop
Pressure Restriction Ind No
Length Segment Isolated 47520
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 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 The operator's actions did not contribute to the cause of the accident.
Employee Drug Test Ind No
Contractor Drug Test Ind No
Cause Material Failure Of Pipe Or Weld
Cause Details Design-, Construction-, Installation-, Or Fabrication-Related
Metallurgical Ind Yes
Failure Type Design-, Construction-, Installation-, Or Fabrication-Related
Other Factor Yes
Other Factor Details Incomplete Penetration Created A Notch Like Stress Concentration Which Allowed F
Pwf Additional Other Ind Yes
Collected Data Ind Yes
Other Tool Tech Ind Yes
Other Tool Def&mfl Tool Runs 12/10/14, Def&mfl Tool Runs 10/19/11, Def&mfl Tool Runs 6/7/06
Other Recent Year 2014
Has Hydrtst Conduc Before Ind No
Direct Asmnt Conducted No
Non Destructive Exam Ind No
Preparer Name K*** P****
Preparer Title Pipeline Safety Supervisor
Preparer Email K*********@n***********.com
Preparer Telephone 316-721-7053
Prepared Date 2016-09-28 00:00:00
Authorizer Name B*** F******
Authorizer Telephone 316-721-7066
Authorizer Title General Manager - Pipeline And Terminal Operations
Authorizer Email B***********@n***********.com
Narrative At 2:28 am on 06-01-2015 the san antonio control center received an ammonia detection alarm and station lockout at the ramah pump station, in iberville parrish, la. A station lockout isolates the station piping from the mainline piping. The control center operator contacted the area nustar employee. The nustar employee arrived at 4:09 am and confirmed the smell of ammonia originating from buried mainline pipe within the pump station and not the station piping. Emergency shutdown procedures for the mainline were started at 0412. The pipeline was completely shut down and blocked at 0421. Nustar's maintenance crew arrived on 06-02-2015, excavated and installed a stopple tee downstream of the leak location. On 06-03-2015 they excavated the pipeline and confirmed the stopple tee fitting as the cause. They completed repairs on 06-03-2015 and the line was restarted at 23:45. The stopple tee fitting will be sent for metallurgical analysis in order to determine the cause of the leak. Results of metallurgical analysis: the leak was caused by a nearly through wall crack in the longitudinal seam weld of the stopple(r) fitting. The crack initiated in an area of misalignment of the cuff edges and incomplete penetration (ip); these are fabrication defects created during installation of the fitting. The ip created a notch-like stress concentration which allowed for the initiation of a crack. The crack propagated until it was nearly through the weld. The remaining intact ligament was unable to contain the internal line pressure.

All rights reserved. Copyright © by ClearPHMSA