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I l <br /> I <br /> Nominal Capacity: 10000 gal. Most Accurate Capisity: 10000 gal. From: Per Customer <br /> � I <br /> I Vapor Recovery System: None <br /> i <br /> i <br /> I Tank Measurements: 129" Bottom to Grade Total Tubing to Assemble 159" <br /> I I <br /> 35" Top to Grade Extend Hose an Suction to 41" <br /> Ii <br /> Is the 411b rule required? No <br /> I <br /> Hight to 12" mark from bottom of tank = 146" <br /> I <br /> Pressure at bottom of tank = 4.69 psi <br /> I Pressure at top of tank 1.67 psi <br /> � I <br /> Tank Diameter: 94" Nater in Tank: None Gallons: 0 <br /> I i <br /> Inventory: Gal. Total <br /> 94" 100M 10000 <br /> Nater (5 10000 I <br /> Top Off 10 10010 <br /> Thermal-Sensor Reading after Circulation: 17320 Between: 75/76 Degrees Diqits: 319 <br /> I <br /> I <br /> Coefficient of Expansion: <br /> Type of Product: Diesel Fuel <br /> i <br /> Hydrometer Employed: 4 H <br /> Term, in Tank after Circulation: 75.0 I <br /> I <br /> Temperature of Gravity Sample: 82 I <br /> Difference: +7 <br /> Observed A.P.1. Gravity: 33.3 Recprccal: 22.02 Page N: 37 <br /> I <br /> Total 9uantity in tank: 10010 Divided by: 2202 = Volume Change in this tank per degree <br /> I � <br /> Volume change in this tan): per degree change: 4.54586739 <br /> Divided by the number of digits: 319 <br /> Test Factor "A" = .0143 <br /> I I <br /> .001 <br /> I I <br /> v <br />