Laserfiche WebLink
r <br />14. <br />'s. Name of Supplier. Owner or <br />C <br />15. TANK TO TEST <br />Identity by position <br />f� <br />Brand and Grade <br />Address No. and Streets) <br />15a. BRIEF DIAGRAM OF TANK FIELD <br />17. ,ILL -UP FOR TEST <br />Stick flow Bottom <br />be" fill -UP �' Im in. <br />to %" Gallons Tank Diameter <br />city <br />16. CAPACITY /wry <br />Nfomind Capacity 101 W <br />Gallons <br />By most gree Q <br />capacity chart available <br />Gallons <br />18: SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK ❑ Water in tank ❑ Une(s) being tested with LVLLT <br />See manual sections applicable. Check below and record procedure in log (27). ❑ High water table in tank excavation <br />Inventory <br />Use maximum allowable test pressure for all teats. 19. TANK MEASUREMENTS FOR <br />Four pound rule does not apply to doublewalied tanks. TSTT ASSEMBLY , <br />Complete section below: <br />Bottom of tank to grade' ............................ In. <br />1. is four pound rule required? <br />2. Height to 12" mark from bottom of tank <br />3. Pressure st bottom of tank <br />4. Pressure at top of tank <br />of burial <br />dia. <br />Yes ❑ No ❑ <br />Add3" for -r probe way ........................... 30.1n. <br />Total tubing to assemble — approximate ............. 'In. <br />20. EXTENSION HOSE SETTING <br />In. <br />*S3in. <br />peclproceJ F s <br />Tank top to grade' .................................. <br />Extend hose on suction tube a" or more <br />P.SI. <br />below tank top ...................................... In. <br />P.S.I. <br />'tt Fill pipe extends above gra, use top of fill. <br />22. Thermal -se sor reading after circulation <br />Ainea <br />The above calculations aro to be used for dry *oil conditions to <br />dish a positive pressureadvantag%orwhen lasing thefour pound <br />rule to compensate for the presence of subsurface water in the tank <br />area. <br />Refer to H.F.PJL 30. Sections 2424 and 2-7.2 and the tank <br />manufacturer regarding allowable system test Rressures. <br />Im <br />kn. <br />In. <br />.¢'Z _ f u'.'b 1 <br />State Date of Test <br />From <br />��❑1i Station Chart <br />�1 Tank Manufacturers Chart <br />�L-11 Company Engineering Data <br />❑ Charts supplied with <br />Other <br />Total Gallons <br />Gallons aa. Reading <br />i' ( O <br />Transfer total to line 25a <br />21. VAPOR RECOVERY SYSTEM ❑ stage I ❑:)toga it <br />24b. COEFFICIENT OF EXPANSION <br />RECIPROCAL METHOD <br />Type of Product ........................................ <br />Hydrometer Employed .................................. H <br />Temperature In Tank <br />After Circulation ........................................ °F <br />Temperature of Sample ................................. °F <br />Di(*/-) ...:..................................... °F <br />:� ► " LO -60 °F <br />Observed A.P.I. Gravity ................................. <br />23. Digas per °F In range of expected change <br />� jBetween <br />6 �7 s <br />peclproceJ F s <br />COEFFICIENT OF EXPANSION (Complete after circulation) <br />24a. Corrected A.P.I. Gravity <br />Total quantity In Reciprocal <br />Volume change in <br />S7`� <br />full tank (16 o' 17) <br />this tank f °F <br />Observed A.P.I. Gravity ................................... <br />r <br />Transfer to Una 28L <br />Hydrometer employed ................................... <br />H <br />Arl. °F <br />24c. FOR TESTING WITH WATER we Table C a D <br />Observed Semple Temperature ......................... <br />Corrected A.P.I. Gravity <br />r S� <br />Waw Temperature atter Circulation60°F. <br />From Table A .................................... <br />TableC ................................................ <br />°F <br />Coefficient of Expansion <br />for Involved Product <br />... �g <br />1 (°3Qd� �,f� <br />Coefficient of Water <br />Table O ....................... <br />From Table 8 ............................................ <br />Transfer COE to Una 25b <br />Added Surfactant? ❑ Yes ❑ No Transfer COE to Una 25b. <br />25. (a) Q QQQO <br />x (b)r f (d�0"ZG _ (Clio a 3a -7b S— <br />gallon <br />Total quantity in <br />Coefficient of expansion for <br />Volume change in this tank <br />fug tank (16 or 17) <br />(a) is ° 01-V -10 S <br />Involved product <br />` 6 Z2 <br />per °F <br />= 10 I 7 oxa Lj <br />Is <br />26. <br />This <br />Volume change per °F (25 or 24b) <br />Digits per °F In Wet <br />Volume change per digtt <br />tea <br />Range (23) <br />Compute to 4 decimal places. <br />factor (a) <br />