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!h <br />14. � e s <t q� �/�co �� - G,) if �,q c Iz - 30 - 97 <br />Owner or Dealer . Address City State Date of Test <br />5 am15. TANK <br />M-" P A <br />CA <br />;.•� Lt�.97.a <br />16. CAPACITY <br />,,00ax- i Nominal Capacity `O f 600 <br />r position Gallons <br />Is there doubt as to True Capacity 7 <br />de See Section "DETERMINING TANK CAPACITY" <br />From <br />Station Chart <br />By most accurate <br />capacity chart available (va `�❑ Tank Manufacturer's Chart <br />Gallons Company Engineering Data <br />Charts supplied with PMT& <br />Other <br />17. FILL -UP FOR TEST <br />Stick Water Bottom <br />before Fill -up <br />to W in. Gallons <br />Fill up. STICK BEFORE AND AFTER EACH COMPARTMENT DROP OR EACH METERED DELIVERY QUANTITY <br />Inventory <br />Tank Diameter W.5 Product in full tank (up to fill pipe) <br />Stick Readings Total Gallons <br />to % In. Gallons ea. Reading <br />103100 /03!00 <br />WARN -0- <br />-- 1 O 3 <br />'ToTA � to& <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 Stage 1 <br />Water in tank ❑ High water table in tank excavation ® Line($) being tested with LVLLT Stage 11 <br />26. <br />30. HYDROSTATIC <br />21. <br />TEMPERATURE/VOLUME FACTOR (a) TO TEST THIS TANK <br />19. TANK MEASUREMENTS FOR <br />39. <br />LOG OF TEST PROCEDURES <br />Observed API Gravity: Temp. 66 IF Corrected API Gravity LLL r <br />TSTT ASSEMBLY <br />14-4 " <br />b,! <br />Bottom of tank to Grade* .................... <br />22. <br />Thermal -Sensor reading after circulation 1 �2l�loz- °F <br />Add 30" for 4" L ................. <br />CHANGE <br />27. <br />dogds Nearest <br />Add 24" for 3" L or air seal ....... <br />32. Product in <br />23. <br />Digits per IF In range of expected change 3z i <br />Total tubing to assemble Approximate ........ <br />/,?o <br />Temperature <br />dlg,ts <br />20. EXTENSION HOSE SETTING <br />i1 C� Ji <br />`'1`' <br />24. <br />10 3(0& x • 00Olo21id l = 6.4415-340049 40049 gallons <br />total quantity in coefficient of expansion for volume change in this tank <br />Tank top to grade* .................................. <br />Thermal <br />Chane <br />D <br />Higher + <br />full tank (16 or 17) involved product per IF . <br />Extend hose on suction tube 6" or more <br />below tank top ..................................... <br />• 5 <br />25. <br />(0-4-415U040 _ 3.14' _ OZOPOP r 0 I This is <br />At los Level compute <br />Change per Hour <br />and running test. (Use full No. <br />length of line if needed. <br />0 I <br />volume change per IF (24) Digits per IF in test Volume change per digit. test <br />' if Fill pipe extends above grade, use top of fill. <br />Sensor <br />Reading <br />D <br />Lower - <br />(c) <br />Range (23) Compute to 4 decimal places. factor (a) <br />26. <br />30. HYDROSTATIC <br />31. <br />34. <br />38. NET VOLUME <br />39. <br />LOG OF TEST PROCEDURES <br />PRESSURE <br />VOLUME MEASUREMENTS( Y) <br />TEMPERATURE COMPENSATION <br />CHANGES <br />ACCUMULATED <br />CONTROL <br />RECORD TO .001 GAL. <br />USE FACTOR (a) <br />EACH READING <br />CHANGE <br />27. <br />28. 29. <br />Standpipe Level <br />32. Product in <br />Product <br />35. <br />36. <br />37. <br />Temperature <br />At High Level record <br />DATE <br />Record details of settingU P Reading <br />in laches <br />Graduate <br />Replaced (-) <br />Thermal <br />Chane <br />D <br />Higher + <br />Computation <br />P <br />c x a = <br />1 1 1 1 <br />i <br />Total End Deflection <br />Beginning Lavelle <br />of which <br />olumem int <br />Volume Minus <br />Expansion (+) or <br />Contraction (-) <br />At los Level compute <br />Change per Hour <br />and running test. (Use full No. <br />length of line if needed. <br />0 I <br />Sensor <br />Reading <br />D <br />Lower - <br />(c) <br />Expansion + <br />Contraction +- <br />Before <br />After <br />Product <br />TIME <br />(24 hr) <br />Reading :i Restored <br />Reading <br />Reading <br />Recovered (+) <br />- <br />,33(V)- 837(T) <br />(HFPA criteria) <br />% <br />t <br />55 <br />E t! 'I of <br />I d <br />S <br />SME" <br />, s <br />c <br />A -P <br />W <br />�N0 WAT&'R MO int i v <br />d. <br />n a <br />11110 I -roOftC 4AMDkc 4 11:1RADLAer 1 II 1 II 1 11 1 11 A . oz0/ I <br />0 <br />1310 5TO RT ,Low L..&U' L.. `7c 1 11 12 11 •1050 <br />132.5 `° Z 13.11 12. • 650 •7(oo 4.110 <br />1340 '/ 3 13.S/ 12. .315'5 ?5 -%.100 <br />1355 101 4 13.q 12. 1 .4T5 .600 4.115 <br />1z <br />700 <br />70? 4 15' 4.10 ©51 <br />-7/4 40 4 .12 ( -- . O2. I 07Z <br />7 19 44 4. p?v 14. d-;5 • 637 <br />5 <br />i �j.� <br />12- <br />�� <br />• %95 4. 0�t5 <br />7z 1 <br />4 3 <br />T . 0&1) <br />4 <br />®�ImIM <br />000 <br />S AM, <br />m <br />• <br />r" <br />Ism <br />- <br />1310 5TO RT ,Low L..&U' L.. `7c 1 11 12 11 •1050 <br />132.5 `° Z 13.11 12. • 650 •7(oo 4.110 <br />1340 '/ 3 13.S/ 12. .315'5 ?5 -%.100 <br />1355 101 4 13.q 12. 1 .4T5 .600 4.115 <br />1z <br />700 <br />70? 4 15' 4.10 ©51 <br />-7/4 40 4 .12 ( -- . O2. I 07Z <br />7 19 44 4. p?v 14. d-;5 • 637 <br />5 <br />i �j.� <br />12- <br />�� <br />• %95 4. 0�t5 <br />7z 1 <br />4 3 <br />T . 0&1) <br />4 <br />Ga H. <br />4 <br />3 <br />