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20. EXTENSION HOSE' SETTING <br />Tank top to grade* .............................. <br />Extend hose on suction tube 6" or more <br />below tank top ................................. <br />If Fill pipe extends above grade, use top of fill. <br />24. X = gallons <br />total quantity in coefficient of expansion for volume change in this tank <br />full tank (16 or 17) involved product per °F <br />25. — — This is <br />volume change per °F (24) Digits per °F in test Volume change per digit. test <br />Range (23) Compute to 4 decimal places. factor (a) <br />26. <br />LOG OF TEST PROCEDURES <br />14. <br />31. <br />VOLUME MEASUREMENTS (Y) <br />RECORD TO .001 GAL. <br />34. <br />TEMPERATURE COMPENSATION <br />USE FACTOR (a) <br />Owner or Dealer Address City State <br />Date of Test <br />D� <br />28. <br />Record details of setting U <br />O P <br />and running test. (Use full <br />length of line if needed.) <br />15. TANK TO TEST <br />16. CAPACITY <br />From <br />Z <br />IV <br />36. <br />Change <br />+ Higher <br />9 <br />Lower - <br />c <br />( 1 <br />37. <br />(amputation <br />c <br />(c) x (a) = <br />Expansion + <br />Contraction - <br />❑ Station Chart <br />At High level record <br />total End Deflection <br />aa� <br />level to <br />which <br />Restored <br />By most accurate <br />At Low level compute <br />Change per Hour <br />(NFPA criteria) <br />m <br />After <br />Reading <br />Product <br />Recovered (+) <br />Nominal Capacity capacity chart available <br />❑ Tank Manufacturer's Chart <br />O <br />Identity by position <br />M <br />Gallons Gallons <br />❑ Company Engineering Data <br />�� <br />Is theredoubt to TCity 7 <br />ouas rue Capacity <br />❑ Charts supplied with petro jitP <br />UGrade <br />See Section "DETERMINING TANK CAPACITY" <br />Other TANK TESTER <br />17. FILL -UP FOR TEST Stick Readings <br />Total Gallons <br />to 1/9 in. <br />Gallons ea. Reading <br />Stick Water Bottom <br />before Fill -up Inventory <br />to Ye in. Gallons <br />Fill up. STICK BEFORE AND AFTER EACH COMPARTMENT DROP OR EACH METERED DELIVERY QUANTITY <br />Tank Diameter Product in full tank (up to fill pipe) <br />18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK <br />VAPOR RECOVERY SYSTEM <br />See manual sections applicable. Check below and record procedure in log (26). Water Observation - Well level <br />❑ Stage I <br />N0 cow <br />CL - 3 <br />❑ Water in tank ❑ High water table in tank excavation ❑ Line(s) being tested with LVLLT <br />Stage II <br />Z -4 <br />n S <br />6 to M <br />21. TEMPERATURE/VOLUME FACTOR (a) TO TEST THIS TANK <br />-4trix <br />19. TANK MEASUREMENTS FOR <br />1 <br />ut p o3i M <br />TSTT ASSEMBLY <br />Observed API Gravity: Temp. °F Corrected API Gravity <br />7 — <br />�p <br />Bottom of tank to Grade* " <br />' ' ' - � ' ' ' � ' ' ' ' ' ' ' <br />22. <br />°F <br />FL _ <br />Thermal -Sensor reading atter circulation <br />' n <br />Add 30" for 4" L <br />digits <br />Nearest <br />Add 24" for 3" L or air seal ....... <br />23. Digits per °F in range of expected change <br />Total tubing to assemble Approximate ........ <br />digits <br />20. EXTENSION HOSE' SETTING <br />Tank top to grade* .............................. <br />Extend hose on suction tube 6" or more <br />below tank top ................................. <br />If Fill pipe extends above grade, use top of fill. <br />24. X = gallons <br />total quantity in coefficient of expansion for volume change in this tank <br />full tank (16 or 17) involved product per °F <br />25. — — This is <br />volume change per °F (24) Digits per °F in test Volume change per digit. test <br />Range (23) Compute to 4 decimal places. factor (a) <br />26. <br />LOG OF TEST PROCEDURES <br />30. HYDROSTATIC <br />PRESSURE <br />CONTROL <br />31. <br />VOLUME MEASUREMENTS (Y) <br />RECORD TO .001 GAL. <br />34. <br />TEMPERATURE COMPENSATION <br />USE FACTOR (a) <br />38. NET VOLUME <br />CHANGES <br />EACH READING <br />39. <br />ACCUMULATED <br />CHANGE <br />27. <br />DATE <br />28. <br />Record details of setting U <br />O P <br />and running test. (Use full <br />length of line if needed.) <br />29. <br />Reading <br />No. <br />Standpipe Level <br />in Inches <br />32. Product in <br />Graduate <br />Product <br />Replaced (-) <br />35. <br />Thermal <br />Sensor <br />Reading <br />36. <br />Change <br />+ Higher <br />9 <br />Lower - <br />c <br />( 1 <br />37. <br />(amputation <br />c <br />(c) x (a) = <br />Expansion + <br />Contraction - <br />Temperature <br />Adjustment <br />I <br />At High level record <br />total End Deflection <br />Beginning <br />of <br />Reading <br />level to <br />which <br />Restored <br />Volume Minus <br />Expansion (+) or <br />Contraction (-) <br />F33(V)- AE37(T) <br />At Low level compute <br />Change per Hour <br />(NFPA criteria) <br />Before <br />Reading <br />After <br />Reading <br />Product <br />Recovered (+) <br />TIME <br />(24 hr.) <br />N <br />M <br />y <br />M <br />IA <br />c <br />r4 <br />-i <br />COO) <br />O <br />0 <br />m <br />3 <br />c <br />O <br />mr <br />O <br />w <br />O <br />0 <br />m <br />m <br />a <br />CD <br />n <br />J <br />m <br />O <br />O <br />O <br />Q <br />m <br />CD CD <br />-n <br />�o o m <br />M = <br />�M <br />x o <br />y Z <br />z <br />3 <br />CD <br />-4 <br />fJ7 <br />a <br />z <br />X <br />,y <br />T <br />A <br />W <br />xa <br />iv y <br />CD <br />-n Z <br />S T <br />30 <br />CD <br />M <br />a <br />CD <br />x <br />v <br />:3 <br />e# <br />r(• <br />Q <br />�J <br />i <br />� ya 7C <br />N p cn <br />M <br />Ate_ <br />y <br />1 <br />� <br />rY_rr�a <br />I� <br />C/�DO <br />\Y <br />CA <br />CO) <br />CD <br />y <br />e�F <br />