SlideShare a Scribd company logo
1 of 34
Line Tightness and Leak Detector Testing
Petro-Tite Line Tightness Tester
July 15, 2015
Chattanooga, Tennessee
Line Tightness Test Requirements
Tennessee UST Regulations
•Must detect 0.1 GPH release at 1 ½ times operating pressure
•Required by rule at installation; Rule 400-18-01-.02(1)(d)6.
•Results must be maintained until next test; Rule 400-18-01-.04(5)(b)
•Required annually for pressurized piping; Rule 400-18-01-.04(2)(b)1.
– Unless site is using monthly monitoring (interstitial monitoring, SIR, electronic
LLD)
Terminology- Pressurized Piping
• Full Pump Pressure
• LLD Holding Pressure
• LLD Metering Pressure
• LLD Opening Time
• Maximum Allowable Bleedback
• Leak Rate in Gallons per Hour
Submersible Pump
Terminology- Continued
Shear Valve
• Safety Device
• Test port
• Properly
Anchored
Petro-Tite Line Tightness
Tester
Petro-Tite Line Tightness Tester
High Pressure Gauge
0-160 PSI
Rarely needs to
exceed 75 PSI for
petroleum
applications
Petro-Tite Line Tightness Tester
Volumetric Burette
Graduated in mL and
gallons
0.1 gallon capacity
DO NOT OVERFILL
Purpora Engineering
“Silver Bullet”
Hoke Valve- controls flow
ON/OFF
Needle Valve- fine adjust
Test Adaptor
Air Eliminator
Hydraulic Hose
Other Testing Systems
Estabrook EZ CHEK
•Uses nitrogen gas
•Can test multiple lines
Acurite Line Tester
Tanknology TLD-1
Tanknology TLD-1
Used only by Tanknology technicians
Uses Nitrogen gas
Preparing to Test
 Site Safety Meeting
 Deactivate sub pump (SAFETY FIRST)
 Connect to line- shear valve at furthest
dispenser
 No ball valve- use “silver bullet”
Site Safety
STP relay stuck in
ON position
ALWAYS
DEACTIVATE STP
at the electrical
panel !
Site Safety cont.
• STP Sumps >4 feet deep (ingress)
• Gasoline Vapors- flammable AND TOXIC
• Displaced oxygen
• Motor Vehicles/Pedestrians
• Cones/Barricades
• PPE- Gloves, vest, glasses, boots
• Partner always recommended
Preparing to Test
• REMOVE LEAK DETECTOR and connect
at the STP when :
– No in-line ball valve present at STP
– Confirming STP leaking into tank (o-rings,
check valve or functional element)
– Testing large or long flex lines
– Bad fittings at shear valve
Common Line Testing Problems
• Bad Functional Element- leaks into tank
• NO BALL VALVE- must test at the tank.
• Satellite Dispensers
• Air/Vapor Pockets
• Piping Deflection (flex pipe)
• Liquid/Vapors in STP sump
Example 1- Temperature Change
o Large Pressure Changes
o Small Volume Changes
o Diminishes to “0” PSI
o SOLUTION- obtain 2-3 readings w/no change; can be prevented by
purging line prior to test.
Time
(Military)
Event Description Pressure (psi) Volume (gallons)
Comments/Actions
(List leaks observed even if repairs are made and retest passes)
Before After Before After Net Change
0800 Begin Line Test 50
0815 21 50 .0850 .0810 -.0040
0830 30 50 .0810 .0780 -.0030
0845 37 50 .0780 .0755 -.0025
0900 42 50 .0755 .0735 -.0020
0915 45 50 .0735 .0720 -.0015
0930 47 50 .0720 .0710 -.0010
0945 49 50 .0710 .0705 -.0005
1000 50 50 .0705 .0705 .0000
Example 2- Pipe Deflection
Time
(Military)
Event Description Pressure (psi) Volume (gallons)
Comments/Actions
(List leaks observed even if repairs are made and retest passes)
Before After Before After Net Change
0940 Begin Line Test 50
0950 43 50 .0655 .0610 -.0045
1000 46 50 .0610 .0570 -.0040
1010 48 50 .0570 .0535 -.0035
1020 49 50 .0535 .0515 -.0020
1030 49.5 50 .0515 .0500 -.0015
1040 49.8 50 .0500 .0490 -.0010
1050 49.9 50 .0490 .0485 -.0005
1100 50 50 .0485 .0485 .0000
o Small Pressure Losses
o Small Volume Losses
o Diminishes to “0” PSI
o Gradual volume changes; 30 minutes-1 hours
o Solution: Conduct Beginning Bleedback Test and stretch line prior to test
Example 3- Air/Vapor Pocket
Time
(Military)
Event Description Pressure (psi) Volume (gallons)
Comments/Actions
(List leaks observed even if repairs are made and retest passes)
Before After Before After Net Change
1400 Begin Line Test 50
1405 46 50 .0910 .0260 -.0065 Re-filled burette
1410 45 50 .0860 .0410 -.0041 Re-filled burette
1415 46.5 50 .0770 .0070 -.0070 Re-filled burette
1420 46.0 50 .0850 .0300 -.055 Re-filled burette
o Small Pressure Changes
o Very Large Volume Changes
o Non-repeating and inconsistent
SOLUTION: End test and purge air from line; locate any potential points of
air (siphon lines, low points in product line, dead ends)
Example 4- High Rate of Leak
Time
(Military)
Event Description Pressure (psi) Volume (gallons)
Comments/Actions
(List leaks observed even if repairs are made and retest passes)
Before After Before After Net Change
1315 Begin Line Test 50
1320 15 50 .0750 .0200 -.0045 Re-filled burette
1325 17 50 .0830 .0260 -.0040 Re-filled burette
1330 14 50 .0910 .0330 -.0035 Re-filled burette
1335 16 50 .0780 .0220 -.0020 Re-filled burette
1340 15 50 .0870 .0320 -.0015 Re-filled burette
o Large Pressure Losses
o Large Volume Losses
o Repeated and Consistent Losses over time
o May have to speed up readings, rapid pressure changes
for large leaks
Testing Mechanical Leak Detectors
Mechanical Line Leak Detectors
(MLLD)
Invented in 1958 by Elmer Deter,
Red Jacket Application Engineer
Alerts operator of nozzle to low
line pressure
MLLD Operation
Electronic Line Leak Detectors
(ELLD)
• Tests line during idle time
• Must simulate a 3.0 GPH leak to test
• Programming must be verified
– Pressure based (Veeder-Root PLLD)
– Flow based (Franklin/OPW)
ELLD Testing
• Activates STP
during idle to
conduct testing
• Secondary
containment may
be required
ELLD Operability
Simulating a Leak
Petro-Tite LLD Test
1) Connect pressure regulator
2) Energize STP, adjust pressure to
10 PSI
3) Adjust Petro-Tite flow rate to 189
ml/min (3 gallons per hour)- black
hoke valve
4) De-energize STP
5) Remove regulator and connect
piping to Petro-Tite system
Petro-Tite LLD Test
5) Reactivate STP; MLLD should stay in
leak test mode (1 gal/minute)
6) Keep STP running and close 3-way valve;
MLLD should close, full flow.
QUESTIONS?
Don Taylor
Environmental Consultant
TDEC- Division of Underground
Storage Tanks
(423) 854-5391
Don.Taylor@tn.gov

More Related Content

What's hot

Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...
Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...
Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...Awais Qureshi
 
"Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr...
"Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr..."Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr...
"Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr...Society of Petroleum Engineers
 
Sampling plans fda
Sampling plans   fdaSampling plans   fda
Sampling plans fdaMajdi Ayoub
 
Asme sec viii div 2
Asme sec viii div 2Asme sec viii div 2
Asme sec viii div 2Jithu John
 
Pressure vessel course by Hossein Sadeghi
Pressure vessel course by Hossein SadeghiPressure vessel course by Hossein Sadeghi
Pressure vessel course by Hossein SadeghiHossein Sadeghi
 
MPD familiarization Presentation april 2016.pptx
MPD familiarization Presentation april 2016.pptxMPD familiarization Presentation april 2016.pptx
MPD familiarization Presentation april 2016.pptxcVNguyn5
 
CONTROL VALVE questions.pdf
CONTROL VALVE questions.pdfCONTROL VALVE questions.pdf
CONTROL VALVE questions.pdfAmiTG34
 
Well abandonment process procedures
Well abandonment process proceduresWell abandonment process procedures
Well abandonment process proceduresDrilling Manual
 
Lab 7 measurement of gel strength of drilling mud sample by rheometer
Lab 7 measurement of gel strength of drilling mud sample by rheometerLab 7 measurement of gel strength of drilling mud sample by rheometer
Lab 7 measurement of gel strength of drilling mud sample by rheometerAwais Qureshi
 
Drilling fluid technology, Oil & Gas Industry
Drilling fluid technology, Oil & Gas IndustryDrilling fluid technology, Oil & Gas Industry
Drilling fluid technology, Oil & Gas IndustryMohamed Rashid
 
Plug & Abandonment
Plug & AbandonmentPlug & Abandonment
Plug & AbandonmentStatoil
 
04 Hpht Gas Migration Co2(4 08 06)
04 Hpht Gas Migration Co2(4 08 06)04 Hpht Gas Migration Co2(4 08 06)
04 Hpht Gas Migration Co2(4 08 06)JRThompson8747
 
PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4
PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4
PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4PetroSync
 

What's hot (20)

Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...
Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...
Lab 11 measurement of resistivity of drilling mud and mud cake using resistiv...
 
How to Avoid Those Common Site Troubles During Commissioning
How to Avoid Those Common Site Troubles During CommissioningHow to Avoid Those Common Site Troubles During Commissioning
How to Avoid Those Common Site Troubles During Commissioning
 
"Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr...
"Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr..."Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr...
"Deepwater Managed Pressure Drilling and Well Drillability, Efficiency and Pr...
 
Sampling plans fda
Sampling plans   fdaSampling plans   fda
Sampling plans fda
 
Packer milling
Packer millingPacker milling
Packer milling
 
DST Tool Presentation.pdf
DST Tool Presentation.pdfDST Tool Presentation.pdf
DST Tool Presentation.pdf
 
Asme sec viii div 2
Asme sec viii div 2Asme sec viii div 2
Asme sec viii div 2
 
04 gas lift_equipment
04 gas lift_equipment04 gas lift_equipment
04 gas lift_equipment
 
Pressure vessel course by Hossein Sadeghi
Pressure vessel course by Hossein SadeghiPressure vessel course by Hossein Sadeghi
Pressure vessel course by Hossein Sadeghi
 
Final Control Element
Final Control ElementFinal Control Element
Final Control Element
 
Well Testing
Well TestingWell Testing
Well Testing
 
MPD familiarization Presentation april 2016.pptx
MPD familiarization Presentation april 2016.pptxMPD familiarization Presentation april 2016.pptx
MPD familiarization Presentation april 2016.pptx
 
CONTROL VALVE questions.pdf
CONTROL VALVE questions.pdfCONTROL VALVE questions.pdf
CONTROL VALVE questions.pdf
 
Well abandonment process procedures
Well abandonment process proceduresWell abandonment process procedures
Well abandonment process procedures
 
Lab 7 measurement of gel strength of drilling mud sample by rheometer
Lab 7 measurement of gel strength of drilling mud sample by rheometerLab 7 measurement of gel strength of drilling mud sample by rheometer
Lab 7 measurement of gel strength of drilling mud sample by rheometer
 
Drilling fluid technology, Oil & Gas Industry
Drilling fluid technology, Oil & Gas IndustryDrilling fluid technology, Oil & Gas Industry
Drilling fluid technology, Oil & Gas Industry
 
Fluoroseal Sleeved Plug Valves
Fluoroseal Sleeved Plug ValvesFluoroseal Sleeved Plug Valves
Fluoroseal Sleeved Plug Valves
 
Plug & Abandonment
Plug & AbandonmentPlug & Abandonment
Plug & Abandonment
 
04 Hpht Gas Migration Co2(4 08 06)
04 Hpht Gas Migration Co2(4 08 06)04 Hpht Gas Migration Co2(4 08 06)
04 Hpht Gas Migration Co2(4 08 06)
 
PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4
PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4
PetroSync - IWCF Well Intervention Pressure Control Level 3 & 4
 

Similar to pressurized piping LLD testing chattanooga 2015

Hydrotest REPORT FOR 4'' 158m Line.
Hydrotest REPORT FOR 4'' 158m Line.Hydrotest REPORT FOR 4'' 158m Line.
Hydrotest REPORT FOR 4'' 158m Line.Emeka Ngwobia
 
Hpv pinton pump test
Hpv pinton pump testHpv pinton pump test
Hpv pinton pump testgrebnesor
 
Control valve presentation
Control valve presentationControl valve presentation
Control valve presentationPrem kumar
 
Hydrostatic pressure testing of PE pipelines (handbook) as per EN805
Hydrostatic pressure testing of PE pipelines (handbook) as per EN805Hydrostatic pressure testing of PE pipelines (handbook) as per EN805
Hydrostatic pressure testing of PE pipelines (handbook) as per EN805Vladimir Popovic
 
CNG Technical & Hydrogen Blending in Natural Gas pipeline.pptx
CNG Technical & Hydrogen Blending in Natural Gas pipeline.pptxCNG Technical & Hydrogen Blending in Natural Gas pipeline.pptx
CNG Technical & Hydrogen Blending in Natural Gas pipeline.pptxRishabh Sirvaiya
 
40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter
40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter
40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow MeterEmerson Exchange
 
d2_400_318_Alzuabi.pdf
d2_400_318_Alzuabi.pdfd2_400_318_Alzuabi.pdf
d2_400_318_Alzuabi.pdfSathiaShekar1
 
How to Select the Right Valve for your Application
How to Select the Right Valve for your ApplicationHow to Select the Right Valve for your Application
How to Select the Right Valve for your ApplicationUBMCanon
 
2020-6_TechPres_Ball.pdf
2020-6_TechPres_Ball.pdf2020-6_TechPres_Ball.pdf
2020-6_TechPres_Ball.pdftuanvuthanh4
 
3340f401g plano de teste delphi
3340f401g plano de teste delphi3340f401g plano de teste delphi
3340f401g plano de teste delphiJunior Iung
 
2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...
2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...
2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...Komandur Sunder Raj, P.E.
 
introduccion a los Inyectores para cromatografía de gases
introduccion a los Inyectores para cromatografía de gasesintroduccion a los Inyectores para cromatografía de gases
introduccion a los Inyectores para cromatografía de gasesLgIrvin
 
Internship Report
Internship ReportInternship Report
Internship ReportMalik Ehsan
 
Prvs 2. asme section i fired vessel rev4
Prvs   2. asme section i fired vessel rev4Prvs   2. asme section i fired vessel rev4
Prvs 2. asme section i fired vessel rev4David Alexandre
 

Similar to pressurized piping LLD testing chattanooga 2015 (20)

Hydrotest REPORT FOR 4'' 158m Line.
Hydrotest REPORT FOR 4'' 158m Line.Hydrotest REPORT FOR 4'' 158m Line.
Hydrotest REPORT FOR 4'' 158m Line.
 
Hpv pinton pump test
Hpv pinton pump testHpv pinton pump test
Hpv pinton pump test
 
Control valve presentation
Control valve presentationControl valve presentation
Control valve presentation
 
Hydrostatic pressure testing of PE pipelines (handbook) as per EN805
Hydrostatic pressure testing of PE pipelines (handbook) as per EN805Hydrostatic pressure testing of PE pipelines (handbook) as per EN805
Hydrostatic pressure testing of PE pipelines (handbook) as per EN805
 
Rotor Insertion Flow Meter Technical Information
Rotor Insertion Flow Meter Technical InformationRotor Insertion Flow Meter Technical Information
Rotor Insertion Flow Meter Technical Information
 
CNG Technical & Hydrogen Blending in Natural Gas pipeline.pptx
CNG Technical & Hydrogen Blending in Natural Gas pipeline.pptxCNG Technical & Hydrogen Blending in Natural Gas pipeline.pptx
CNG Technical & Hydrogen Blending in Natural Gas pipeline.pptx
 
40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter
40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter
40 CFR 98 Tier 4 Greenhouse Gas Reporting with Stack Emissions Flow Meter
 
NONG YAO PROJECT SUBSEA VALVE Rev 0
NONG YAO PROJECT SUBSEA VALVE Rev 0NONG YAO PROJECT SUBSEA VALVE Rev 0
NONG YAO PROJECT SUBSEA VALVE Rev 0
 
d2_400_318_Alzuabi.pdf
d2_400_318_Alzuabi.pdfd2_400_318_Alzuabi.pdf
d2_400_318_Alzuabi.pdf
 
How to Select the Right Valve for your Application
How to Select the Right Valve for your ApplicationHow to Select the Right Valve for your Application
How to Select the Right Valve for your Application
 
Vortex flow meter manual
Vortex flow meter manualVortex flow meter manual
Vortex flow meter manual
 
2020-6_TechPres_Ball.pdf
2020-6_TechPres_Ball.pdf2020-6_TechPres_Ball.pdf
2020-6_TechPres_Ball.pdf
 
Pipininspect
PipininspectPipininspect
Pipininspect
 
2 delugevalve a
2 delugevalve a2 delugevalve a
2 delugevalve a
 
3340f401g plano de teste delphi
3340f401g plano de teste delphi3340f401g plano de teste delphi
3340f401g plano de teste delphi
 
2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...
2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...
2007 ASME Power Conference Troubleshooting Condenser Vacuum Issues At North O...
 
introduccion a los Inyectores para cromatografía de gases
introduccion a los Inyectores para cromatografía de gasesintroduccion a los Inyectores para cromatografía de gases
introduccion a los Inyectores para cromatografía de gases
 
Internship Report
Internship ReportInternship Report
Internship Report
 
Prvs 2. asme section i fired vessel rev4
Prvs   2. asme section i fired vessel rev4Prvs   2. asme section i fired vessel rev4
Prvs 2. asme section i fired vessel rev4
 
Lessons learned solving pilot valve instability issues on LNG storage tanks
Lessons learned solving pilot valve instability issues on LNG storage tanksLessons learned solving pilot valve instability issues on LNG storage tanks
Lessons learned solving pilot valve instability issues on LNG storage tanks
 

pressurized piping LLD testing chattanooga 2015

  • 1. Line Tightness and Leak Detector Testing Petro-Tite Line Tightness Tester July 15, 2015 Chattanooga, Tennessee
  • 2. Line Tightness Test Requirements Tennessee UST Regulations •Must detect 0.1 GPH release at 1 ½ times operating pressure •Required by rule at installation; Rule 400-18-01-.02(1)(d)6. •Results must be maintained until next test; Rule 400-18-01-.04(5)(b) •Required annually for pressurized piping; Rule 400-18-01-.04(2)(b)1. – Unless site is using monthly monitoring (interstitial monitoring, SIR, electronic LLD)
  • 3. Terminology- Pressurized Piping • Full Pump Pressure • LLD Holding Pressure • LLD Metering Pressure • LLD Opening Time • Maximum Allowable Bleedback • Leak Rate in Gallons per Hour
  • 6. Shear Valve • Safety Device • Test port • Properly Anchored
  • 8. Petro-Tite Line Tightness Tester High Pressure Gauge 0-160 PSI Rarely needs to exceed 75 PSI for petroleum applications
  • 9. Petro-Tite Line Tightness Tester Volumetric Burette Graduated in mL and gallons 0.1 gallon capacity DO NOT OVERFILL
  • 10. Purpora Engineering “Silver Bullet” Hoke Valve- controls flow ON/OFF Needle Valve- fine adjust Test Adaptor Air Eliminator Hydraulic Hose
  • 11. Other Testing Systems Estabrook EZ CHEK •Uses nitrogen gas •Can test multiple lines
  • 13. Tanknology TLD-1 Tanknology TLD-1 Used only by Tanknology technicians Uses Nitrogen gas
  • 14. Preparing to Test  Site Safety Meeting  Deactivate sub pump (SAFETY FIRST)  Connect to line- shear valve at furthest dispenser  No ball valve- use “silver bullet”
  • 15. Site Safety STP relay stuck in ON position ALWAYS DEACTIVATE STP at the electrical panel !
  • 16. Site Safety cont. • STP Sumps >4 feet deep (ingress) • Gasoline Vapors- flammable AND TOXIC • Displaced oxygen • Motor Vehicles/Pedestrians • Cones/Barricades • PPE- Gloves, vest, glasses, boots • Partner always recommended
  • 17. Preparing to Test • REMOVE LEAK DETECTOR and connect at the STP when : – No in-line ball valve present at STP – Confirming STP leaking into tank (o-rings, check valve or functional element) – Testing large or long flex lines – Bad fittings at shear valve
  • 18. Common Line Testing Problems • Bad Functional Element- leaks into tank • NO BALL VALVE- must test at the tank. • Satellite Dispensers • Air/Vapor Pockets • Piping Deflection (flex pipe) • Liquid/Vapors in STP sump
  • 19. Example 1- Temperature Change o Large Pressure Changes o Small Volume Changes o Diminishes to “0” PSI o SOLUTION- obtain 2-3 readings w/no change; can be prevented by purging line prior to test. Time (Military) Event Description Pressure (psi) Volume (gallons) Comments/Actions (List leaks observed even if repairs are made and retest passes) Before After Before After Net Change 0800 Begin Line Test 50 0815 21 50 .0850 .0810 -.0040 0830 30 50 .0810 .0780 -.0030 0845 37 50 .0780 .0755 -.0025 0900 42 50 .0755 .0735 -.0020 0915 45 50 .0735 .0720 -.0015 0930 47 50 .0720 .0710 -.0010 0945 49 50 .0710 .0705 -.0005 1000 50 50 .0705 .0705 .0000
  • 20. Example 2- Pipe Deflection Time (Military) Event Description Pressure (psi) Volume (gallons) Comments/Actions (List leaks observed even if repairs are made and retest passes) Before After Before After Net Change 0940 Begin Line Test 50 0950 43 50 .0655 .0610 -.0045 1000 46 50 .0610 .0570 -.0040 1010 48 50 .0570 .0535 -.0035 1020 49 50 .0535 .0515 -.0020 1030 49.5 50 .0515 .0500 -.0015 1040 49.8 50 .0500 .0490 -.0010 1050 49.9 50 .0490 .0485 -.0005 1100 50 50 .0485 .0485 .0000 o Small Pressure Losses o Small Volume Losses o Diminishes to “0” PSI o Gradual volume changes; 30 minutes-1 hours o Solution: Conduct Beginning Bleedback Test and stretch line prior to test
  • 21. Example 3- Air/Vapor Pocket Time (Military) Event Description Pressure (psi) Volume (gallons) Comments/Actions (List leaks observed even if repairs are made and retest passes) Before After Before After Net Change 1400 Begin Line Test 50 1405 46 50 .0910 .0260 -.0065 Re-filled burette 1410 45 50 .0860 .0410 -.0041 Re-filled burette 1415 46.5 50 .0770 .0070 -.0070 Re-filled burette 1420 46.0 50 .0850 .0300 -.055 Re-filled burette o Small Pressure Changes o Very Large Volume Changes o Non-repeating and inconsistent SOLUTION: End test and purge air from line; locate any potential points of air (siphon lines, low points in product line, dead ends)
  • 22. Example 4- High Rate of Leak Time (Military) Event Description Pressure (psi) Volume (gallons) Comments/Actions (List leaks observed even if repairs are made and retest passes) Before After Before After Net Change 1315 Begin Line Test 50 1320 15 50 .0750 .0200 -.0045 Re-filled burette 1325 17 50 .0830 .0260 -.0040 Re-filled burette 1330 14 50 .0910 .0330 -.0035 Re-filled burette 1335 16 50 .0780 .0220 -.0020 Re-filled burette 1340 15 50 .0870 .0320 -.0015 Re-filled burette o Large Pressure Losses o Large Volume Losses o Repeated and Consistent Losses over time o May have to speed up readings, rapid pressure changes for large leaks
  • 24. Mechanical Line Leak Detectors (MLLD) Invented in 1958 by Elmer Deter, Red Jacket Application Engineer Alerts operator of nozzle to low line pressure
  • 26.
  • 27.
  • 28. Electronic Line Leak Detectors (ELLD) • Tests line during idle time • Must simulate a 3.0 GPH leak to test • Programming must be verified – Pressure based (Veeder-Root PLLD) – Flow based (Franklin/OPW)
  • 29. ELLD Testing • Activates STP during idle to conduct testing • Secondary containment may be required
  • 32. Petro-Tite LLD Test 1) Connect pressure regulator 2) Energize STP, adjust pressure to 10 PSI 3) Adjust Petro-Tite flow rate to 189 ml/min (3 gallons per hour)- black hoke valve 4) De-energize STP 5) Remove regulator and connect piping to Petro-Tite system
  • 33. Petro-Tite LLD Test 5) Reactivate STP; MLLD should stay in leak test mode (1 gal/minute) 6) Keep STP running and close 3-way valve; MLLD should close, full flow.
  • 34. QUESTIONS? Don Taylor Environmental Consultant TDEC- Division of Underground Storage Tanks (423) 854-5391 Don.Taylor@tn.gov