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Pop *21 - 5 <br />'TE PREPARATION AND SYSTEM DATA <br />CHECK TANK SYSTEM SIZE 1 -TANK 2 - TANK = 3 - TANK <br />CUSTOMER: DATE: <br />LOCATION NO.: SYSTEM NO.: <br />CITY/STATE: PRODUCT: <br />SITE PREPARATION <br />I OTHER CONDITIONS <br />t!; <br />00 �WGS 0 RISERS <br />VAPOR RECOVERY D`NO PREPARATION OTHER_ <br />VENT TO ATMOSPHERE 0 P -V VALUE REMOVED' 0 OTHER <br />OREMOTE/SUBMERSIBLE (DEPTH 1 <br />'0--,WCTION (HEIGHT <br />CHECK VALVE <br />STRAINER <br />IMPACT VALVE <br />CHECK V E <br />STRAINER <br />SUCTION CONNECTION <br />0 REMOVED & OPEN <br />1� IN PLACE <br />CLOSED <br />REMOVED &COVER <br />R REPLACED <br />0 OTHER <br />0 REMOVED <br />21-N PLACE <br />0 REMOVED &COVER <br />❑ REPLACED <br />CIOTHER <br />CLOSED <br />E�77s <br />PLUG-IN <br />❑ PLUG OUT 0 CLOSED <br />❑ OPEN <br />OBURIED <br />0 EXTRACTABLE <br />0 REMOVED <br />❑1:1 IN PLACE <br />ED & <br />REREPLACED <br />❑ CAP REPLACED <br />QOTHER <br />MOVED <br />'M <br />0 IN PLACE <br />OV <br />7 0 COV <br />0 REMOVED & COV <br />REPLACED <br />CIOTHER <br />0 UNION <br />0 COUPLING <br />1P0P EN WITH FOIL <br />EN <br />00-0 NO FOIL <br />0 IN PLACE <br />A T ERD <br />Gauge Other (SP*Cify) <br />IN <br />M <br />one <br />T. PROBE <br />LR 37 <br />—6-10 <br />TEST I DATA <br />CALIBRATION <br />TANK I <br />TANK 2 TANK 3 r <br />LOCATION <br />LOCATION <br />DROP TUBE <br />LOCATION DROP TUBE LOCATION <br />DROP TUBE <br />FILL <br />Other (SPeCify) <br />IN <br />OUT I None <br />FILL <br />Gauge Other (SPOCIfy) IN OUT <br />Non q FILL <br />Gauge Other (SP*Cify) <br />IN <br />OUT <br />one <br />T. PROBE <br />LR 37 <br />—6-10 <br />LEE <br />CALCULATION' <br />TC <br />COEFF1 CIENT OF EXPANSION 1/.F <br />=ADIVISION <br />BALANCE <br />37 <br />e7� <br />TC <br />GT CE <br />cc IN OUT <br />TANK I <br />TANK 2 <br />TANK 3 <br />TOTAL <br />CALIBRATION <br />LEVELS LOCATION <br />li <br />METHOD LIQUID <br />LS SOLID ROD <br />LEAK RATE ILR) CALCUEXTION <br />Time <br />Tank I <br />Tank 2 <br />Tank 3 <br />1 <br />2 3 4 <br />5 <br />6 <br />AVERAGE <br />ISTART <br />11ViO <br />110/3 <br />MINUTE <br />cc's <br />LR 37 <br />—6-10 <br />LEE <br />CALCULATION' <br />TC <br />COEFF1 CIENT OF EXPANSION 1/.F <br />=ADIVISION <br />J�/- �- 3f Sl�' <br />37 <br />e7� <br />AVG.CC'S/DIV. <br />LEAK RATE ILR) CALCUEXTION <br />DIVISIONS <br />cc <br />cc <br />OR <br />TIME <br />LR = X <br />CALIBRATION, <br />IN OUT <br />AMIN TE <br />DIVISION <br />MINUTE <br />LR 37 <br />3 <br />TEMPERATURE COMPENSATIOIWfTC) <br />CALCULATION' <br />TC <br />COEFF1 CIENT OF EXPANSION 1/.F <br />TANK I TANK 2 TANK 3 <br />3785 A*F <br />SYSTEM CAPACITY. <br />GALLONS <br />TC <br />GT CE <br />cc IN OUT <br />TANK I <br />• <br />GRAVITY — TEMPERATURE, F <br />OR <br />TIME <br />SOURCE OT159C <br />MINUTE <br />OA '0 D 0 CHART <br />013 0 E . 0 PUBLISHED DATA AT 60OF <br />0 c 0 OTHER <br />TC <br />TANK I TANK 2 TANK 3 <br />SYSTEM CAPACITY. <br />GALLONS <br />GT <br />TC <br />TANK I <br />TANK 2 <br />TANK 3 <br />TOTAL <br />a*F, <br />t Temp. Differential <br />A*F <br />_yT Time of Temp. <br />Differentia=l, Min.ATime <br />L__L <br />din <br />I <br />ABSOLUTE LEAK RATE IALR) CALCULATION <br />ABSOLUTE LEAK RATE 3 377, g2l <br />LEAK RATE TEMP. COMPENSATION CC/MIN <br />X <br />cc/MIN GAWHOUR <br />cl it: ALR > f 0.05 GPH, A CHECK TEST WAS CONDUCTED WHICH CONFIRMS THE ABOVE RESULTS (CALCULATIONS ON CHART) <br />0 A CHECK TEST WAS NOT CONDUCTED. <br />60 MINUTES/HOUR 3785 CC/GALLON - 0.015852 <br />