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.." � . 14.�' ,'� 1 1 � �.=o4f�..K�s tl'�4� s ;•l� .� *���d �. ._ p :7 't, ..,i-t�"��.1.....�..� •.� at ---------J,Date of Tea, <br /> Naas of Suppiw.Owner of Dealer Address No.and Straetla) City St <br /> 15a. BRIEF DIAGRAM OF TANK FIELD 16. CAPACITY From <br /> � 1�5. TANK TO TEST ❑ Station chart <br /> Nominal Capacity <br /> yL ar® � _.,---_-_--,-.--.__— ❑ Tank Manufacturer's Chart <br /> m i `K arrt , la <br /> Identity by position Gallons <br /> �1��s asp Company Engineering Data <br /> Qw_7—d' ✓, By most accurate ❑ Charts supplied with <br /> Brand and Grade capacity chart available -- '�"' _-_�J_------- ❑ Other ----------_._------_.-.—.----- <br /> Gallons <br /> Total Gallons <br /> 11. FILL-UP FOR TEST Gallons ea.Reading <br /> a a � . <br /> Suck water Bosom a 1 / <br /> before Full-upIn. Inventory _ —_ --- --- - - ----- <br /> to a" Gallons Tank Diameter <br /> 18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK ❑Water in tank ❑ Une(s)being tested with LVLLT l <br /> Sea manual searons applicable.Check below and record procedure In log 127). ❑High water table in lank excavation <br /> Lae maximum alio btuir teat prassure for all testa. 19. TANK MEASUREMENTS FOR Transfar total to line 2 a <br /> Four pound rule doe`not apply to doutdewaned tank`. TSTT ASSEMBLY <br /> 21. VAPOR RECOVERY SYSTEM IA stage f L.l stags 11 <br /> Complete►action bal". ' <br /> - Bosom of lank to grade' .......... ) "'•� <br /> Add 30"for"T•probe&say........................... so in. 24b. COEFFICIENT OF EXPANSION <br /> I is four pound rule requited, Yea ❑ No ❑ Total tubing to assemble—approximate..... ....... in RECIPROCAL METHOD <br /> Type of Product ................... <br /> —in 20. EXTENSION HOSE SETTING i . <br /> 2 Height t0 12"mark from bottom of tank Hydrometer Employed ----H <br /> Tank top to grade'.................................. ---------.in. <br /> Extend hose on suction lube 6"or more Temperature in Tank <br /> 3. Pressure at bosom of lank P.S.I. Atter Circulation........................................ '_'_°F <br /> below lank top...................................... _ _in. ..., <br /> .............................. <br /> 'It Fill pipe extends above grade,use top of fill. Temperature of Sample ... <br /> 4. Presbure&t top of tank P.S.I. , (.�',, <br /> 22. Thermal-Sensor reading atter circulation I- 7-F <br /> Difference('/-)............... ......••..... '•' °F <br /> digits Q in. —iL dig Observed A.P.I.GravyDepen Of Dural y .........................e1vto <br /> 23. Digits per°F In range of expected change — Reciprocal!4 rPage a <br /> digits { t 1 <br /> Tank the. -in. <br /> COEFFICIENT OF EXPANSION (Complete after circulation) <br /> 24a. Corrected A.P.I.Gravity Total quantity in Reciprocal Volume change in <br /> lull lank 116 or 17) this tank per°F <br /> Water table in. Observed to Line 26a. <br /> aervedA.P.1.Gravity................................... — <br /> NOTES: <br /> Hydrometer employed...................................---_H <br /> 24c. FOR TESTING WITH WATER see Table C it D <br /> Observed Sample Temperature ......................... ----__----°F <br /> Corrected A.P.I.Gravity Water Temperature after Circulation <br /> 60°F,From Table A.................................... _--- Table C ................................................ °F <br /> Coefficient of Expansion Coefficient of Water <br /> The above calculations are to be used for dry wil conditions to for Involved Product Table D ................................................ _—_---- <br /> apositwepressure advantage,or when using the four pound From Table 8........................................... ---r <br /> rub m <br /> to compensate for the presence of subsurface water In ler terik Transfer COE to Line 25b. Added Surfactant? ❑Vas 1-1 No Transfer COE to Line 25b. <br /> area. <br /> fiiffer to N.F.PA. 30. Sections 2-3.24 and 2-7.2 and the tank 25. L1 x (b) = 1=1--_ — gallons <br /> manufacturer regwding akowabb Wiliam teat pressures. Total quantity In Coefficient of expansion for Volume change In this tank <br /> full tank(16 or 17) involved product per°F <br />