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tM�YJ"' I <br /> j Nominal Capacity: 3000 gal. Most Accurate Capisity: 3('d U gal. Fran: Per Qs+rv•e <br /> vapor Recovery System: None g E E <br /> 'i Tank Measurements-, 132" Bottom to Grade Total Tubing to Assemble 162" E OCT 4 1 <br /> M9 <br /> 9 <br /> �0n <br /> li 57" Top to Grade Extend Fuse on Suction to 63" ENVIRONMENTAL,HEALTH <br /> j Is the 416 rule required? No PERMIT/SERICES <br /> j, Hight to 12" mark from bottom of tank. = 148" <br /> j <br /> j Pressure at bottom of tank = 4.75 psi <br /> Pressure at top of tank 2.34 psi <br /> i I <br /> Tank, Diaseter: 75" Mater in Tank: None Gallons: 0 <br /> j Inventory: Gal. Total <br /> j 75" 3000 3000 <br /> Mater 0 3000 <br /> j Top Off 10 3010 <br /> Thermal-Sensor Reading after Circulation: 17735 Between: 76/77 Degrees Digits: 319 <br /> Coefficient of Expansion: <br /> I <br /> j Type of Product: Diesel Fuel <br /> j Hydrometer Employed: 4 H <br /> Temp. in Tank after Circulation: 76,4 <br /> I <br /> j Temperature of Gravity Sample: 82 <br /> j Difference: +6 <br /> � Observed A.P.I. Gravity: 3.3 Recprocal: 2201 Page 0: 37, <br /> j <br /> j <br /> j Total Quantity in tank: 3010 Divided by: 2201 = volume Change in this tank per degree <br /> j <br /> Volume change in this tank per degree change: 1.36756020 <br /> j Divided by the number of digits: 319 <br /> f <br /> I <br /> Test Factor "A" _ .0043 <br /> j <br />