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;ja.. Mo_t. Accurate Ca iFit{: 11627 gal. FrowF <br />niIlne=' fitil=ita <br />Vapor Recovery f y wi ew,; N01 iL <br />Tani-, Measurements: 142" Bottom to Grade o 172" <br />47" Top to Grade Entci)d base or, iuLUo;� r'," <br />Is the 41b rule required? No <br />I <br />Hight to 12" mark from bottom of tank: <br />c <br />Pressure at bottom of tank = ?.6 p51 <br />Pressure at top of tank MO psi <br />Tank Diameter- 95" Water in Tank: None Gallons: O <br />Inventory- Gal. lutal <br />95" 11627 11627 <br />Water 0 11627 <br />Top Ott 20 11647 <br />Thermal -Sensor Reading after Circulation: 18:26 between% 77/78 Opgrees DiA�it� <br />Coefficient of Expansion; <br />Type of Product: Gasoline <br />Hydrometer Employed- 6H <br />�Q <br />Temp. w Tank: after Circulation: 77.8 <br />Temperature of Gravity Sample., -'9 <br />:iii e ei,ce: +1 <br />Ubserved'A.P.i.'brevity. page #i r,2 <br />Total Quantity in tank: 116 � Divided by. 1492 = Volume Change in this tank per degree <br />A <br />Volum change in this t�,;;`, pw- d+ tjree change: 7.W,6,10027 <br />Divided by the <br />Test Factor "i'A" s .02U <br />h <br />I <br />