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Popp •3.5 <br />SITE REPARATI N AND SYSTEM DATA <br />CHECK TANK SYSTEM SIZE t - TANK M 2 - TANK = 3. TANK <br />CUSTOMER: DATE' 2 ` -Z/-98 <br />LOCATION NO.: 6011 <br />CITY/STATE: 1-610/ �A <br />SYSTEM NO.: <br />PRODUCT: s eo[? X116 <br />SITE PREPARATION <br />VAPOR RECOVERY ❑ PLUGS LJ RISERS ����❑ OTHER <br />VENT ❑ NO PREPARATION I.&rOPEN TO ATMOSPHERE ❑ P•V VALUE REMOVED Ir OTHER <br />UQREMOTE/SUBMERSIBLE (DEPTH 1 <br />❑ SUCTION (HEIGHT 1 <br />CHECK VALVE <br />STRAINER <br />IMPACT VALVE <br />CHECK VALVE <br />STRAINER <br />SUCTION CONNECTION <br />REMOVED & OPEN <br />❑REMOVED <br />❑CLOSED <br />❑BURIED <br />❑REMOVED <br />❑UNION <br />�❑ <br />3kN' PLACE <br />LYlIN PLACE <br />❑ CLOSED <br />LUG <br />❑ EXTRACTABLE <br />❑ IN PLACE <br />❑ COUPLING <br />❑CLOSED <br />❑REPLACED "COVER <br />OUT <br />�EN <br />❑REMOVED <br />❑REP ACED&COVER <br />❑OPEN WITH FOIL <br />&COVER <br />❑REPLACED <br />❑REMOVED <br />OTHER <br />Z; V- <br />❑ IN PLACE <br />❑OTHER <br />❑ OPEN NO FOIL <br />TANK 3 <br />TANK 2 <br />TANK 3 <br />® CAP REREMVPLACED <br />aF� <br />❑ IN PLACE <br />❑OTHER <br />.... <br />± Temp. Differential <br />° <br />a Time <br />❑ OTHER <br />❑ OTHER <br />T Time of Temp. <br />60 <br />Differential, Min. <br />1 <br />TEST 1 DATA <br />CALIBRATION <br />LEVELS LOCATION Lr"/ / L <br />f 6• <br />TANK t TANK 2 TANK 3 <br />LOCATION <br />DROP TUBE LOCATION <br />DROP TUBE LOCATION DROP TUBE <br />FILL <br />Gauge Other (Specify) <br />IN <br />OUT None FILL <br />Gauge Other (Specify) <br />IN OUT <br />Norm FILL <br />Gauge Other (Specify) IN OUT <br />None <br />T. PROBE <br />e�Me <br />'140 <br />-,*-14 % ^ 144 6 I DG <br />—leo <br />14 Cp <br />END /I;LfCi <br />TC = 'Z /r V I/ <br />Q DIVISION <br />BALANCE <br />'4 71 <br />zvjr, Zzr -Z6 <br />Z7 <br />Z; V- <br />GT <br />Q°F <br />TC- <br />TANK 3 <br />TANK 2 <br />CALIBRATION <br />LEVELS LOCATION Lr"/ / L <br />f 6• <br />M TROD SOLID ROO ❑ LIQUID <br />Time <br />Tank 1 <br />Tank 2 <br />Tank 3 <br />1 <br />2 <br />3 4 5 <br />6 <br />AVERAGE <br />START � <br />�.% <br />CC'S <br />e�Me <br />'140 <br />-,*-14 % ^ 144 6 I DG <br />—leo <br />14 Cp <br />END /I;LfCi <br />TC = 'Z /r V I/ <br />Q DIVISION <br />2.C.3 <br />'4 71 <br />zvjr, Zzr -Z6 <br />Z7 <br />Z; V- <br />AVG. CC'S/DIV. yf o fF5 <br />LEAK RATE (LR) CALCULATtON <br />LR - ±A DIVISIONS X CALIBRATION, CC - CC IN OUT <br />AMINUTE DIVISION MINUTE <br />LR- lZoe Y71 <br />TEMPERATURE COMPENSATION iTC1 CALCULATION <br />COEFFICIENT OF EXPANSION 1/ °F a a44K <br />3785 GT CE A°F CC IN OUT <br />GRAVITY <br />TEMPERATURE, F <br />TC _ _ <br />OR <br />TIME MINUTE (+) (- i <br />SOURCE ❑ T159C <br />❑ A <br />❑ D ❑ CHART <br />❑ B <br />❑ E ❑ PUBLISHED DATA AT 60OF <br />❑ C <br />❑ OTHER <br />TC = 'Z /r V I/ <br />TANK 1 TANK 2 TANK.3 <br />SYSTEM CAPACITY, <br />GALLONS <br />�f?d <br />GT <br />Q°F <br />TC- <br />TANK 3 <br />TANK 2 <br />TANK 3 <br />TOTAL <br />aF� <br />.... <br />± Temp. Differential <br />° <br />a Time <br />T Time of Temp. <br />60 <br />Differential, Min. <br />1 <br />1 <br />ABSOLUTE LEAK RA+T�E (ALR) CALCULATION <br />t <br />ABSOLUTE LEAK RATE ,� / B 7-71 w - r <br />LEAK RATE TEMP. COMPENSATION CC/ 1 <br />n., <br />= eI X 0.015652 <br />CC/MIN GAL/HOU R <br />❑ IF ALR i ± 0.05 GPH, A CHECK TEST WAS CONDUCTED WHICH CONFIRMS THE ABOVE RESULTS (CALCULATIONS ON CHART) <br />❑ A CHECK TEST WAS NOT CONDUCTED. <br />. 60 MINUTES/HOUR _ 3765 CC/GALLON - 0.015852 <br />