HL incident on 2023-08-04 — KS

Operator
Chs Mcpherson Refinery Inc.
Cause
Corrosion Failure
Commodity
Refined And/or Petroleum Product (Non-Hvl) Which Is A Liquid At Ambient Conditions
Program
HL
Damage and Injuries
0 fatalities 0 injuries
Property damage (nominal)
$20,000
Incident datetime
2023-08-04 00:00 UTC
Report number
Location
KS
Narrative
Operators responding to lel alarms in well #9 vicinity observed liquid product at the ground surface above known ngl piping. Operators isolated the piping segment by closing nearby valves, which stopped the release. Vacuum trucks were utilized to de-inventory all affected piping. The soil near the release location was excavated and affected piping was exposed to determine the leak location. A pin hole was identified by visual inspection. The pinhole is located in a segment of piping that is not at a low point. The affected deadleg was eliminated by cutting out the tee at the branch connection and the failed pipe was sent for third party metallurgical analysis. The analysis determined that aqueous corrosion was the likely cause of failure. Chsmri plans to take the following steps to identify further corrosion impacts to the effected piping circuits: 1. Perform inspection of dead leg piping and develop plan to remove piping. 2. Evaluate products for active corrosion contributions. 3. Perform additional inspections on non-dead leg piping. 4. Where possible, flush dead legs on a quarterly basis. 5. Perform hydrotest after dead leg removal.
Detailed record list
Report Received Date
2023-08-04 00:00:00
Iyear
2023
Report Number
20230177
Supplemental Number
39020
Report Type
Supplemental Final
Operator Id
Name
Chs Mcpherson Refinery Inc.
Operator Street Address
2000 S. Main
Operator City Name
Mcpherson
Operator State Abbreviation
KS
Operator Postal Code
67460
Time Zone
Central
Daylight Savings Ind
Yes
Location Latitude
Location Longitude
Commodity Released Type
Refined And/or Petroleum Product (Non-Hvl) Which Is A Liquid At Ambient Conditions
Commodity Subtype
Other
Commodity Details
Natural Gasoline
Unintentional Release Bbls
2.38
Recovered Bbls
2.38
Fatality Ind
No
Fatal
0
Injury Ind
No
Injure
0
Accident Identifier
Scada-Based Information (Such As Alarm(S), Alert(S), Event(S), And/or Volume Or Pack Calculations)
System Part Involved
Onshore Equipment And Piping Associated With Belowground Storage
On Off Shore
Onshore
Status When Identified
Normal Operation, Includes Pauses Between Batches And During Maintenance
Shutdown Due Accident Ind
Yes
Still Shutdown Ind
Yes
Communication State Fed Ind
Yes
Party Initiated Communication
Operator
Nrc Rpt Num
Additional Nrc Report Numbers
1372960
Ignite Ind
No
Notify Qualified Indiv Ind
Yes
Oil Spill Removal Org Ind
No
Num Pub Evacuated
0
Pipe Fac Name
Chs Mri Conway Storage Terminal
Segment Name
#4 Ngl Facility Piping
Onshore State Abbreviation
Ks
Onshore Postal Code
67460
Onshore City Name
Not Within A Municipality
Onshore County Name
Mcpherson
Designated Location
Milepost
Designated Name
Conway Term
Federal
No
Location Type
Totally Contained On Operator-Controlled Property
Incident Area Type
Underground
Incident Area Subtype
Under Soil
Depth Of Cover
36
Crossing
No
Pipe Facility Type
Intrastate
Item Involved
Pipe
Pipe Type
Pipe Body
Puddle Weld Ind
No
Pipe Diameter
4
Pipe Wall Thickness
0.235
Pipe Smys
60000
Pipe Specification
A53b
Pipe Seam Type
Seamless
Pipe Manufacturer
Unknown
Pipe Coating Type
Fusion Bonded Epoxy(Fbe)
Coating Applied Ind
Unknown
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
Yes
Commodity Reached Hca
No
Est Cost Oper Paid
0
Est Cost Gas Released
400
Est Cost Prop Damage
20000
Est Cost Emergency
5000
Est Cost Environmental
90000
Est Cost Other
500
Est Cost Other Details
Costs To Compile And Submit Phmsa Report.
Prpty
115900
Num Persons Hosp Not Ovnght
0
Num Injured Treated By Emt
0
Num Resident Building Affctd
0
Num Business Building Affctd
0
Accident Psig
168
Mop Psig
720
Mop Cfr Section
Component Design Pressure �195.406(A)(2)
Maop Established Date
2011-10-06 00:00:00
Maop Reversal Flow Ind
No
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
Yes
Scada Conf Ind
Yes
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
Controller responded according to procedure and implemented corrective actions per plans. Failure due to piping corrosion and not related to controller activity.
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 Water Acid Ind
Yes
Int Metallurgical Basis Ind
Yes
Int Dead Leg Loc Ind
Yes
Corrosion Inhibitors
No
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
Yes
Hydrtst Most Rcnt Year
2019
Hydrtst Most Rcnt Pressure
1025
Direct Asmnt Conducted
No
Non Destructive Exam Ind
No
Intrnl Cor Wtr Drpout Acid Ind
Yes
Preparer Name
M******* S*****
Preparer Title
Principal Dot Compliance
Preparer Email
M**************@c*****.com
Preparer Telephone
4066285293
Preparer Fax
4066285293
Prepared Date
2023-12-27 00:00:00
Local Contact Name
B**** P*****
Local Contact Email
B***********@c*****.com
Local Contact Telephone
620-241-9251
Authorizer Name
G*** B****
Authorizer Telephone
4066285200
Authorizer Title
Vp Pipelines And Terminals
Authorizer Email
G*********@c*****.comc
Narrative
Operators responding to lel alarms in well #9 vicinity observed liquid product at the ground surface above known ngl piping. Operators isolated the piping segment by closing nearby valves, which stopped the release. Vacuum trucks were utilized to de-inventory all affected piping. The soil near the release location was excavated and affected piping was exposed to determine the leak location. A pin hole was identified by visual inspection. The pinhole is located in a segment of piping that is not at a low point. The affected deadleg was eliminated by cutting out the tee at the branch connection and the failed pipe was sent for third party metallurgical analysis. The analysis determined that aqueous corrosion was the likely cause of failure. Chsmri plans to take the following steps to identify further corrosion impacts to the effected piping circuits: 1. Perform inspection of dead leg piping and develop plan to remove piping. 2. Evaluate products for active corrosion contributions. 3. Perform additional inspections on non-dead leg piping. 4. Where possible, flush dead legs on a quarterly basis. 5. Perform hydrotest after dead leg removal.
Report Received Date 2023-08-04 00:00:00
Iyear 2023
Report Number 20230177
Supplemental Number 39020
Report Type Supplemental Final
Operator Id 26065 PHMSA Enforcement
Name Chs Mcpherson Refinery Inc.
Operator Street Address 2000 S. Main
Operator City Name Mcpherson
Operator State Abbreviation KS
Operator Postal Code 67460
Time Zone Central
Daylight Savings Ind Yes
Location Latitude 38.37043 Google Maps OpenStreetMap
Location Longitude -97.7825 Google Maps OpenStreetMap
Commodity Released Type Refined And/or Petroleum Product (Non-Hvl) Which Is A Liquid At Ambient Conditions
Commodity Subtype Other
Commodity Details Natural Gasoline
Unintentional Release Bbls 2.38
Recovered Bbls 2.38
Fatality Ind No
Fatal 0
Injury Ind No
Injure 0
Accident Identifier Scada-Based Information (Such As Alarm(S), Alert(S), Event(S), And/or Volume Or Pack Calculations)
System Part Involved Onshore Equipment And Piping Associated With Belowground Storage
On Off Shore Onshore
Status When Identified Normal Operation, Includes Pauses Between Batches And During Maintenance
Shutdown Due Accident Ind Yes
Still Shutdown Ind Yes
Communication State Fed Ind Yes
Party Initiated Communication Operator
Nrc Rpt Num 1372782 NRC Report How to search
Additional Nrc Report Numbers 1372960
Ignite Ind No
Notify Qualified Indiv Ind Yes
Oil Spill Removal Org Ind No
Num Pub Evacuated 0
Pipe Fac Name Chs Mri Conway Storage Terminal
Segment Name #4 Ngl Facility Piping
Onshore State Abbreviation Ks
Onshore Postal Code 67460
Onshore City Name Not Within A Municipality
Onshore County Name Mcpherson
Designated Location Milepost
Designated Name Conway Term
Federal No
Location Type Totally Contained On Operator-Controlled Property
Incident Area Type Underground
Incident Area Subtype Under Soil
Depth Of Cover 36
Crossing No
Pipe Facility Type Intrastate
Item Involved Pipe
Pipe Type Pipe Body
Puddle Weld Ind No
Pipe Diameter 4
Pipe Wall Thickness 0.235
Pipe Smys 60000
Pipe Specification A53b
Pipe Seam Type Seamless
Pipe Manufacturer Unknown
Pipe Coating Type Fusion Bonded Epoxy(Fbe)
Coating Applied Ind Unknown
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 Yes
Commodity Reached Hca No
Est Cost Oper Paid 0
Est Cost Gas Released 400
Est Cost Prop Damage 20000
Est Cost Emergency 5000
Est Cost Environmental 90000
Est Cost Other 500
Est Cost Other Details Costs To Compile And Submit Phmsa Report.
Prpty 115900
Num Persons Hosp Not Ovnght 0
Num Injured Treated By Emt 0
Num Resident Building Affctd 0
Num Business Building Affctd 0
Accident Psig 168
Mop Psig 720
Mop Cfr Section Component Design Pressure �195.406(A)(2) View CFR 49 §192
Maop Established Date 2011-10-06 00:00:00
Maop Reversal Flow Ind No
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 Yes
Scada Conf Ind Yes
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 Controller responded according to procedure and implemented corrective actions per plans. Failure due to piping corrosion and not related to controller activity.
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 Water Acid Ind Yes
Int Metallurgical Basis Ind Yes
Int Dead Leg Loc Ind Yes
Corrosion Inhibitors No
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 Yes
Hydrtst Most Rcnt Year 2019
Hydrtst Most Rcnt Pressure 1025
Direct Asmnt Conducted No
Non Destructive Exam Ind No
Intrnl Cor Wtr Drpout Acid Ind Yes
Preparer Name M******* S*****
Preparer Title Principal Dot Compliance
Preparer Email M**************@c*****.com
Preparer Telephone 4066285293
Preparer Fax 4066285293
Prepared Date 2023-12-27 00:00:00
Local Contact Name B**** P*****
Local Contact Email B***********@c*****.com
Local Contact Telephone 620-241-9251
Authorizer Name G*** B****
Authorizer Telephone 4066285200
Authorizer Title Vp Pipelines And Terminals
Authorizer Email G*********@c*****.comc
Narrative Operators responding to lel alarms in well #9 vicinity observed liquid product at the ground surface above known ngl piping. Operators isolated the piping segment by closing nearby valves, which stopped the release. Vacuum trucks were utilized to de-inventory all affected piping. The soil near the release location was excavated and affected piping was exposed to determine the leak location. A pin hole was identified by visual inspection. The pinhole is located in a segment of piping that is not at a low point. The affected deadleg was eliminated by cutting out the tee at the branch connection and the failed pipe was sent for third party metallurgical analysis. The analysis determined that aqueous corrosion was the likely cause of failure. Chsmri plans to take the following steps to identify further corrosion impacts to the effected piping circuits: 1. Perform inspection of dead leg piping and develop plan to remove piping. 2. Evaluate products for active corrosion contributions. 3. Perform additional inspections on non-dead leg piping. 4. Where possible, flush dead legs on a quarterly basis. 5. Perform hydrotest after dead leg removal.

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