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Page 5 <br /> SITE PREPARATION AND SYSTEM DATA <br /> THREE-TANK SYSTEM <br /> CUSTOMER: /�� DATE. r a 9 <br /> LOCATION NO.: 2ez, SYSTEM NO.: <br /> *CITY/STATE: STV G/e Ta1Y PRODUCT: <br /> SITE PREPARATION <br /> OTHER CONDITIONS <br /> VAPOR RECOVERY ❑ PLUGS EZ giSERS ❑ OTHER <br /> VENT ❑ NO PREPARATION EL1 PEN TO ATMOSPHERE ❑ P-V VALUE REMOVED ❑ OTHER <br /> ailiEMOTE/SUBMERSIBLE (DEPTH 1 ❑ SUCTION (HEIGHT <br /> CHECK VALVE STRAINER IMPACT VALVE CHECK VALVE STRAINER SUCTI CONNECTION <br /> ❑ <br /> REMOVED&OPEN ❑REMOVED ❑CLOSED El ❑BURIED REMOVED ❑UNION <br /> L:. 0 PLACE EZPr5LACE ❑CLOG LOSD ❑EXTRACTABLE ❑IN PLACE ❑COUPLING <br /> ❑CLOSED ❑RREMOVED EPLACED&COVER Z{ d EN ❑REMOVED ❑RE LACED&COVER ❑OPEN WITH FOIL <br /> ❑REMOVED&COVER El IN PLACE —]OPEN NO FOIL <br /> REPLACED ❑OTHER REMOVEOTHER <br /> E]CAP REPLD& D ❑IN PLACE <br /> ❑OTHER <br /> ❑OT ❑OTHER <br /> TEST 1 DATA <br /> TANK 1 TANK 2 TANK 3 <br /> LOCATION DROP TUBE LOCATION DROP TUBE LOCATIO DROP TUBE <br /> FILL Gauge Other(Specify) IN OUT None FILL Gauge Other(Specify) IN OUT Non Gauge Other(Specify) IN OUT None <br /> T.PROBE <br /> BALANCE <br /> CALIBRATION <br /> LEVELS LOCATION / METHOD / <br /> Lam' SOLID ROD ❑ LIQUID <br /> Time Tank 1 Tank 2 ank 3 1 2 3 4 ,y.. 5 6 AVERAGE <br /> START L ,6 cc's /�J <br /> END DIVISION �/� Z l I 1 Ul7 16 <br /> AVG.CC'S/DIV. z q <br /> LEAK RATE (L11) A U A <br /> LR= ±A DIVISIONS X CALIBRATION, CC = CC IN OUT <br /> MINUTE DIVISION MINUTE <br /> LR= t13, 00 0' <br /> TEMPERATURE COMPENSATION (TC)CALCULATION <br /> COEFFICIENT OF EXPANSION 1/.F 1 <br /> 3785 GT CE A*F CC IN OUT <br /> GRAVITY TEMPERATURE,oF TC - = OR <br /> SOURCE ❑T159C TIME MINUTE <br /> [3A [3D ❑ CHART <br /> ❑ B ❑ E ❑ PUBLISHED DATA AT 60°F <br /> ❑ C ❑ OTHER TC = / Y/I�� <br /> TANK 1 TANK 2 7 <br /> SYSTEM CAPACITY,GALLONS /Q,000 GT TANK 1 TANK 2 TANK.f T <br /> °°F t o3Y A*F <br /> ±Temp. Differential / TC= <br /> T Time of Temp. /S Time <br /> 6 <br /> Differential, Min. <br /> ABSOLUTE LEAK RATE (ALR)CALCULATION <br /> ABSOLUTE LEAK RATE = t 00 v — r / =—/, /Y7 <br /> _.LEAK RATE TEMP.COMPENSATION vCC/MIN <br /> � /7 X 0.015852 <br /> CC/MIN GAL/HOUR <br /> ❑ IF ALR 1 ± 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 />