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Page 5 <br />E-� <br />SITE PREPARATION AND SYSTEM DATA <br />THREE -TANK SYSTEM <br />N DATE: — FS <br />h <br />CUSTOMERS <br />SYSTEM NO.: <br />7SZ <br />LOCATION NO.; yr <br />PRODUCT: <br />CITY/STATE: <br />SITE PREPARATION <br />OTHER CONDITIONS <br />❑ PLUGS RISERS ❑OTHER OTHER <br />VAPOR RECOVERY �EN TO ATMOSPHERE ElP-V VALUEMOVED,RE❑ <br />❑ NO PREPARATION <br />VENT-. <br />1 ❑ SUCTION (HEIGHT <br />(REMCHECK VALVE OTE/SUBMERSIBLE (DEPTH STRAINER SUCTIO NNECTION <br />STRAINER IMPACT VALVE ❑UNION <br />CHECK VALVE ❑ REMOVED <br />CLOSED ❑ BURIED <br />RE VED & OPEN ❑ REMOVED PLUG-IN ❑ COUPLING <br />.. ❑ CLOSED ❑ EXTRACTABLE IN PLACE <br />IN PLACE IN PLACE PLUG -OUT REM -D & COVER El OPEN WITH FOIL <br />(�EN ❑REMOVED ❑ R ACED <br />❑ REMOVE D &COVER OPEN NO FOIL <br />❑CLOSED ❑ IN PLACE OTHER— <br />❑ OTREMOVED & ❑ tN PLACE <br />REPLACED &COVER HER ❑ CAP REPLA <br />❑OTHER <br />❑ OTHER <br />❑ OTH <br />TEST 1 DATA <br />TANK 3 <br />TANK 1 TANK 2 DROP TUBE <br />LOCATION <br />DROP TUBE LOCATI <br />DROP TUBE <br />LOCATION Gauge Other (Specify) IN OUT None <br />FILL Gauge Other (Specify) IN OUT None FILL Gauge Other (Specify) IN OUT No <br />T. PROBE <br />BALANCE <br />CALIBRATION <br />METHOD �/ ❑ LIQUID <br />LOCATION I C>" SOLID ROD <br />LEVELS 3 4 5 6 AVERAGE <br />1 2 <br />r <br />Time Tank 1 Tank 2 T k 3 <br />' • / CC'S ? q 7_ / % �/ < /__SI <br />STARTI <br />END Z•�v 0 DIVISION ee'�� <br />AVG. CC'S/DIV. J, <br />LEA A_ L A U <br />CC IN OUT <br />±CC <br />6 DIVISIONS X CALIBRATION, MINUTE <br />LR DIVISION <br />OMINUTE <br />3 <br />TEMPERATURE COMPENSATION (TC) CALCULATION <br />Qo CC. IN OUT <br />ClC 6 3785 GT CE F _ OR <br />COEFFICIENT OF EXPANSION 1/*F o TC = MINUTE <br />GRAVITY <br />TEMPERATURE, F' D TIME <br />SOURCE ❑T159C / <br />❑ ❑CHART <br />❑ A D <br />❑ E ❑f—.�7 'Z <br />❑ PUBLISHED DATA AT 60°F TC = <br />B <br />❑ B ❑ OTHER ce, <br />TANK 1 TANK 2 TANK 1 ` 4.' 1 TOTAL <br />GT <br />TANK 1 TANK 2 <br />I : C!� vQC� <br />SYSTEM CAPACITY, GALLONS ) APR n <br />` Q� F TC <br />A of = J 17 <br />± <br />To Differential QTime <br />T Time of Temp• b "�i,,� I <br />Diff(ALR) CALCULATION <br />erential, Min. ggSOLUTE LEAK RATE { <br />i-•_ _ N <br />ABSOLUTE LEAK RATE _ e�CC/MI <br />LEAK RATE TEMP. GOMPENSA N <br />4/!5,3 X 0.015852 ° GAL/ <br />HOUR <br />__--- <br />CC/MIN <br />±. .05 GPH, A CHECK TEST WAS CONDUCTED LATIONS ON CHART) <br />WHICH CONFIRMS THE ABOVE RESULTS (CALCU <br />❑ IF ALRi 0 <br />A CHECK TEST WAS NOT CONDUCTED. <br />* 60 MINUTES/HOUR 3785 CC/GALLON = 0.015852 <br />