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14. <br />Owner or Dealer <br />Da 15. TANK TO TEST <br />z <br />rri <br />-y-4 O Identity <br />M <br />I� Grade <br />Address <br />16. CAPACITY <br />Nominal Capacity <br />Gallons <br />Is there doubt as to True Capacity 7 <br />See Section "DETERMINING TANK CAPACITY" <br />City <br />State <br />Date of Test <br />From <br />LJ <br />Station Chart <br />most accurate <br />TEMPERATURENOLUME FACTOR (a) TO TEST THIS TANK <br />ca <br />capacity chart available Ll <br />Tank Manufacturer's Chart <br />Gallons U <br />Company Engineering Data <br />Standpipe Level <br />in Inches <br />Charts supplied with petro Tit! <br />TANK TESTER <br />TSTT ASSEMBLY <br />Other <br />17. FILL -UP FOR TEST Stick Readings Total Gallons <br />to Ve in. Gallons ea. Reading <br />Stick Water Bottom <br />before Fill -up Inventory <br />to Ve 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 VAPOR RECOVERY SYSTEM <br />See manual sections applicable. Check below and record procedure in log (26). Water Observation - Well level Ej Stage I <br />N r co L <br />a On 3 Water in tank High water table in tank excavation E] Line(s) being tested with LVLLT El Stage II <br />• <br />°° <br />30. HYDROSTATIC <br />PRESSURE <br />CONTROL <br />31 • VOLUME MEASUREMENTS (Y) <br />RECORD TO .001 GAL. <br />21. <br />TEMPERATURENOLUME FACTOR (a) TO TEST THIS TANK <br />cn <br />19. TANK MEASUREMENTS FOR <br />28. <br />Record details of settingU 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 />V N m <br />00 p <br />TSTT ASSEMBLY <br />35. <br />Thermal <br />Sensor <br />Reading <br />36. <br />Change <br />Nigher + <br />Lower - <br />(c) <br />Observed API Gravity: Temp. °F Corrected API Gravity <br />Temperature <br />P <br />Adjustment <br />Bottom of tank to Grade* <br />Beginning <br />of <br />Reading <br />22. <br />°F <br />a <br />Before <br />Reading <br />After <br />Reading <br />Product <br />Recovered (+) <br />Thermal -Sensor reading after circulation <br />z <br />Add 30" for 4" L <br />" <br />digits Nearest <br />z <br />Add 24" for 3" L or air seal ....... <br />z <br />23. <br />Digits per -F in range of expected change <br />m <br />Mia <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 • VOLUME MEASUREMENTS (Y) <br />RECORD TO .001 GAL. <br />34' TEMPERATURE COMPENSATION <br />USE FACTOR (a) <br />38• NET VOLUME <br />CHANGES <br />EACH READING <br />�39.ACCUMULATED <br />CHANGE <br />27. <br />DATE <br />28. <br />Record details of settingU 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 />Nigher + <br />Lower - <br />(c) <br />37. <br />Computation <br />(c) x (a) = <br />Expansion+ <br />Contraction- <br />Temperature <br />P <br />Adjustment <br />At Nigh 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 />#33(V)—N37(T) <br />At Low Level compute <br />Change per Hour <br />(NFPAcriteria) <br />Before <br />Reading <br />After <br />Reading <br />Product <br />Recovered (+) <br />TIME <br />(24 hr.) <br />z <br />z <br />m <br />P <br />m <br />Mia <br />n � <br />`G <br />w <br />� a <br />M <br />CA <br />c <br />•r-1 <br />H <br />"1 -4 -4 <br />411, m 0, <br />x a <br />of <br />m <br />or <br />m <br />m <br />a <br />o' m <br />O <br />7 <br />m <br />O Z <br />T <br />v <br />z <br />3 <br />M <br />Q7 <br />n <br />z <br />W <br />DI w <br />'71 <br />co <br />M <br />H <br />M <br />Cn <br />•v <br />T <br />O <br />CCD) = <br />CD <br />x n <br />a <br />m <br />ns <br />y <br />o <br />S <br />a <br />Z Mn <br />z <br />T <br />1 <br />CD <br />c <br />M <br />s0 <br />S <br />_ <br />m <br />_ <br />-� <br />z D <br />CCA <br />z <br />z <br />m <br />P <br />m <br />Mia <br />T <br />v D <br />m a <br />to O. <br />4 <br />a <br />n O <br />D <br />N <br />m <br />m <br />w <br />m <br />jwT <br />_n <br />'Z Z <br />� <br />O <br />P <br />n � <br />`G <br />w <br />� a <br />3 <br />a <br />O <br />3 <br />0 <br />FT <br />• <br />wv` <br />W <br />SIF <br />�s <br />O <br />�rtrri� <br />y <br />1 <br />CD <br />cp <br />CDO <br />CA <br />W <br />co <br />y <br />r� <br />