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14. �-oma 011-1 c30/ /64HO-MAI 400tt_ Loot' t <br />21. <br />9-9 <br />Name of Supplier, Owner or Dealer Address No. and Street(s) City <br />State <br />Date of Test <br />DZ7 <br />15. TANK TO TEST 16. CAPACITY <br />23. <br />From <br />digits <br />change 308 <br />f <br />/v /0000 By most accurate <br />3 i 0I <br />8` <br />Station Chart <br />Tank Manufacturer's Chart <br />r„ <br />O <br />l Nominal Capacity capacity chart available <br />Identity by position Gallons <br />Gallons <br />Company Engineering Data <br />Tank top to grade* ................................. EXTENSION HOSE SETTING <br />Tan. <br />Extend hose on suction tube 6" or more <br />below tank top ..................................... <br />M <br />Is there doubt as to True t Capacity 7 <br />9 8 a (� <br />total quantity in <br />full tank (16 or 17) <br />_ �/ ! �3 t0 �./ / 3 <br />Charts supplied with PPtrO TItP <br />= �; 9a 3�.��3 gallons <br />volume change in this tank <br />per °F <br />o <br />— I Q l t0 / This is <br />hBrand <br />and Grade See Section "DETERMINING TANK CAPACITY" <br />E]Other a"e rEsra <br />volume change per °F (24) <br />Digits per °F in test <br />Range (23) <br />Volume change per digit. test <br />Compute to 4 decimal places. factor (a) <br />26. <br />LOG OF TEST PROCEDURES <br />30. HYDROSTATIC <br />PRESSURE <br />CONTROL <br />17. FILL -UP FOR TEST <br />Stick Readings <br />Total Gallons <br />39 ACCUMULATED, <br />CHANGE <br />27. <br />DATE <br />•• <br />to '/a in. <br />Gallons ea. Reading <br />Standpipe Level <br />in Inches <br />32, Product in <br />Graduate <br />Stick Water Bottom <br />before <br />before Fill O <br />9 / •' <br />�,� <br />37. <br />Computation <br />(c) x (a) = <br />Expansion + <br />Contraction - <br />Temperature <br />Adjustment <br />-up _ Inventory <br />Beginning <br />D D <br />of <br />Reading <br />Levelto <br />which <br />Restored <br />Volume Minus <br />Expansion (+) or <br />Contraction (-) <br />M33(V)- M37(T) <br />At low Level compute <br />Chan Per Hour <br />(NFPA criteria) <br />to '/a in. Gallons <br />_/-'Jo o <br />/Q <br />Product <br />Recovered (+) <br />• <br />Fill up. STICK BEFORE AND AFTER EACH COMPARTMENT DROP OR EACH METERED DELIVERY QUANTITY <br />I <br />I <br />o <br />Tank Diameter •' Product in full tank (up to fill pipe) — <br />ad_4bevc 6-�- fo is " MA <br />8 a 6 <br />o <br />-k <br />o p <br />• <br />18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK Nydb P1 Jf!•3 ® %0 <br />VAPOR RECOVERY SYSTEM <br />p C) <br />1 O n D <br />L <br />See manual sections applicable. Check below and record procedure in log (26). Cent' T d Gi �8•a g 0 d� <br />Stage I <br />Z (A <br />D 3 ry <br />E] Water in tank High water table in tank excavation ❑ Line(s) being tested with LVLLT ' <br />Stage 11 <br />DD,m <br />21. <br />TEMPERATURE/VOLUME FACTOR (a) TO TEST THIS TANK <br />19. TANK MEASUREMENTS FOR <br />TSTT ASSEMBLY <br />Bottom of tank to Grade* .. . . • . . . . <br />•r <br />/3a <br />Is Today Warmer? [I Colder? [ j —° F Product in Tank _° F Fill -up Product on Truck ° F Expected Change ( + or - ) <br />Iq 7 41 61x-83 F <br />22• Thermal -Sensor reading after circulation ° <br />Add 30" for 4" L ................. <br />Add 24" for 3" L or air seal ....... <br />— " <br />23. <br />Digits per °F in range of expected <br />digits <br />change 308 <br />Nearest <br />Total tubing to assemble Approximate ....... . <br />tg •• rr <br />digits <br />Tank top to grade* ................................. EXTENSION HOSE SETTING <br />Tan. <br />Extend hose on suction tube 6" or more <br />below tank top ..................................... <br />i// •' <br />`7' <br />/O •r <br />- ' <br />24. <br />25. <br />9 8 a (� <br />total quantity in <br />full tank (16 or 17) <br />_ �/ ! �3 t0 �./ / 3 <br />x . o00 (0008 a <br />coefficient of expansion for <br />involved product <br />_ U <br />= �; 9a 3�.��3 gallons <br />volume change in this tank <br />per °F <br />o <br />— I Q l t0 / This is <br />' If Fill pipe extends above grade, use top of fill. <br />volume change per °F (24) <br />Digits per °F in test <br />Range (23) <br />Volume change per digit. test <br />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 V) <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 />Higher + <br />Lower - <br />(c) <br />37. <br />Computation <br />(c) x (a) = <br />Expansion + <br />Contraction - <br />Temperature <br />Adjustment <br />At High Level record <br />Total End Deflection <br />Beginning <br />D D <br />of <br />Reading <br />Levelto <br />which <br />Restored <br />Volume Minus <br />Expansion (+) or <br />Contraction (-) <br />M33(V)- M37(T) <br />At low Level compute <br />Chan Per Hour <br />(NFPA criteria) <br />TIME <br />(24 hr,) <br />Before <br />Reading <br />After <br />Reading <br />Product <br />Recovered (+) <br />• <br />I <br />I <br />