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CUSTOMER: <br />LOCATION NO.: <br />E PREPARATION'AND SYSTEM DA Iqw <br />THREE -TANK SYSTEM <br />DATE: <br />SYSTEM NO.: J UN 2 6 1989 <br />CITY/STATE: PRODUCT: <br />SITE PREPARATION <br />OTHER CONDITIONS <br />VAPOR RECOVERY ❑ PLUGS ❑ RISERS El -OTHER <br />VENT ❑ NO PREPARATION El OPEN TO ATMOSPHERE ❑ P -V VALUE REMOVED ❑OTHER <br />❑ REMOTE/SUBMERSIBLE (DEPTH I <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 />Gauge <br />❑ UNION <br />❑ IN PLACE <br />❑ CLOSED <br />❑ REPLACED&COVER <br />❑ OTHER <br />❑ IN PLACE <br />❑ REPLACED &`COVER <br />❑OTHER <br />[]CLOSED <br />PLUGOUT <br />❑ OPEN <br />❑ EXTRACTABLE <br />I❑ REMOVED <br />LJ IN PLACE <br />❑ CAP REPLDACED <br />0 -1 -N --PLACE <br />0IN PLACE <br />❑ REPLACED& COVER <br />MOTHER <br />❑ COUPLING <br />❑ OPEN WITH FOIL <br />�❑OPOPEN NO FOIL <br />E iN PLACE <br />OUT <br />None <br />T. PROBE <br />❑ OTHER <br />SYSTEM CAPACITY, GALLONS <br />❑ OTHER <br />GT <br />= <br />S <br />END <br />TEST 1 DATA <br />CALIBRATION <br />TANK 1 TANK 2 TANK 3 <br />LOCATION <br />DROP TUBE LOCATION <br />DROP TUBE LOCATION <br />DROP TUBE <br />FILL <br />Gauge <br />other (Specify) <br />IN <br />OUT <br />None FILL <br />Gauge <br />Other (Specify) <br />IN <br />OUT <br />None FILL <br />Gauge <br />Other (Specify) <br />IN <br />OUT <br />None <br />T. PROBE <br />SYSTEM CAPACITY, GALLONS <br />� � , <br />GT <br />= <br />S <br />END <br />TANK 3 <br />TOTAL <br />OF <br />A DIVISION <br />��� <br />�5 <br />c/`( <br />BALANCE <br />Temp. <br />= Temp. Differential <br />TC <br />T Time of Temp. <br />ATime <br />Differential, Min, <br />CALIBRATION <br />[ AVG. CC'S/DIV. `d ? <br />A DIVISIONS CC CC <br />LR = X CALIBRATION, _ <br />A�MII^N /TE DIVISION MINUTE <br />IN OUT <br />TEMPERATURE COMPENSATION (TC) CALCULATION // _71 -'- <br />COEFFICIENT OF EXPANSION 1/ °F } <br />LEVELS LOCATION <br />METHOD <br />" ❑ <br />° <br />SOLID ROD LIQUID <br />GRAVITY TEMPERATURE, F <br />Time <br />Tank 1 <br />Tank 2 <br />Tank 3 <br />1 <br />2 <br />3 <br />4 <br />5 <br />6 <br />AVERAGE <br />START <br />: 7 (� <br />TC = S <br />TANK TANK <br />CC'S <br />SYSTEM CAPACITY, GALLONS <br />� � , <br />GT <br />= <br />S <br />END <br />TANK 3 <br />TOTAL <br />OF <br />A DIVISION <br />��� <br />�5 <br />c/`( <br />Temp. <br />= Temp. Differential <br />[ AVG. CC'S/DIV. `d ? <br />A DIVISIONS CC CC <br />LR = X CALIBRATION, _ <br />A�MII^N /TE DIVISION MINUTE <br />IN OUT <br />TEMPERATURE COMPENSATION (TC) CALCULATION // _71 -'- <br />COEFFICIENT OF EXPANSION 1/ °F } <br />o <br />A OUT <br />° <br />TC = 3785 GT CE F CC IN <br />GRAVITY TEMPERATURE, F <br />= OR <br />SOURCE ❑T159C <br />A TIME MINUTE <br />❑ A ❑ D ❑ CHART <br />❑ B ❑ E ❑ PUBLISHED DATA AT 60OF <br />❑ <br />(A✓ <br />C ❑ OTHER <br />TC = S <br />TANK TANK <br />SYSTEM CAPACITY, GALLONS <br />� � , <br />GT <br />= <br />TANK 1 <br />- TANK 2 <br />TANK 3 <br />TOTAL <br />OF <br />4 � a � <br />A°F <br />Temp. <br />= Temp. Differential <br />TC <br />T Time of Temp. <br />ATime <br />Differential, Min, <br />At$bULU I t LEAK RATE IALRI CALCULATION <br />ABSOLUTE LEAK RATE <br />LEAK RATE TEMP. COMPENSATION CC/MiN <br />X 0.015852 * =, c�'v <br />CC/MIN GAL/HOUR <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 - 3785 CC/GALLON - 0.015852 <br />