COMPLIANCE INFO_1985-1998 - Laserfiche WebLink

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14 ��C®.rc) #.i/3 yDl KFTTl�/L1.9.�(% LA�UE LODE Gid Z9 St✓NE$$ Name of supplier. Owner or Dealer Address No. end Bttaat (2) City I State Date of Teat 15. TANK TO TEST 15a. BRIEF DIAGRAM,OF T NK FIELD 5 E� AT'T�c Nry'D Identity by position 4p 1A Uitl LEAD �1i Brsnd and Grade 17, FILL -UP FOR TEST Stick Wolof Bonern bolero Fm.up 0' in. to %' •4' 9S kt. Galbns Talk Diameter 16. CAPACITY Nominal Capacity /94 00 Gallons +.r By most accurate / /, +y{ 2_9 Capacity char) available G• Ge f albns 18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK 11 7W.&tor In lank M.Insla) being tolled with LVLLT See manual sections applicable. Check below and record procedure In tog 127). t39tigh water table in tank excavation Lite lo8.1mum allowable test pressure for an testa. Four pound ruts does not apply to doublewaned sense. COmplate section below; .. I Is lour pound rule required? Yes 0 No ❑ 2 Height to 12- mark from bottom of lank tot. 7, pressure at bottom of lank q,13 P.S.1. A. Pressure at top of isn't 1 of burial dia. r table NOTES: Inventory 19. TANK MEASUREMENTS FOR TSTT ASSEMBLY Q Bottom of tank to grade' ....................... ..... +� In. AddOto• for 'T' probe easy ........................... 30 in. Total tubing to assemble — approximate ............. A68 In. 20. EXTENSION HOSE SETTING' - . y Tank too to grade' .................................. In. Extend hose on auction lube 6' Of more / below tank top ...................................... In. 11,14 PAL •11 Fill pips extends above grade• use lop of fill aSiat 22. Thermsl•Sensor reading after circulation ❑ y3 ❑ digits 7/- 7Z IF In. Charts supplied with Between Zs ............................................ 23. Digits per IF in range o1 expected change digits '_EFFICIENT OF EXPANSION (Complete alter circulation) --in. .✓CJ r2_4 orrected A.P.1.Oravity lo �ssrved A P..t3ravhy................................... C (c) The above calculations ere to be used lot dry sell conditions to establish a positive pressure advantage, or when wing the lour pound rule to compensate IW the presence of subsurface water In the lank area. Ftefer to N.F.P.A. 30. Sections 2.3.2.4 and 2.7.2 and the tank manufacturer regarding affowabfe system 1091 pressures. Hydrometerampbyed...�.�........................... H Observed Sample Temperature ....:b.\...... •F Corrected AA 1. Gravity WF, From Table A ..................................... From Total Gallons aSiat on Chart ❑ Tank Manufacturer's Chart ❑ Company Engineering Dais ❑ Charts supplied with ❑ ............................................ Transfer total to line 2509 Other _ 24b. COEFFICIENT OF EXPANSION RECIPROCAL METHOD Typo of Product ........................................ Hydrometer Employed .................................. H Temperature In Tank 7 %• 2— After Circulation ........................................ •F Temperature of Sample ................................. 70.0-. F Difference (r/-) ......................................... — / IF Observed A.P.I. Gravity y. .................................. nociprocat / y 79 Page a "' z 1/ e el9 /y79 8. 011 y9 9 Total quantity In Reciprocal Volume change In full lank 116 or 17) this tank per IF Transfer to Line 26C - 24c. FORTSi< TING WITH WATER sea Table C a o Water Temperature alter, Clfculllon Table C ............ ...... ............ IF Coefficient of Expansion Total Gallons Gallons as. Madkq 9Q5',�,^ / 18729 T®/ Q From $obis 8 '0 ............................................ Transfer total to line 2509 Added Surloctanll ❑ Yes ❑ No 21. VAPOR RECOVERY SYSTEM ® stage i JZ Stage is 24b. COEFFICIENT OF EXPANSION RECIPROCAL METHOD Typo of Product ........................................ Hydrometer Employed .................................. H Temperature In Tank 7 %• 2— After Circulation ........................................ •F Temperature of Sample ................................. 70.0-. F Difference (r/-) ......................................... — / IF Observed A.P.I. Gravity y. .................................. nociprocat / y 79 Page a "' z 1/ e el9 /y79 8. 011 y9 9 Total quantity In Reciprocal Volume change In full lank 116 or 17) this tank per IF Transfer to Line 26C - 24c. FORTSi< TING WITH WATER sea Table C a o Water Temperature alter, Clfculllon Table C ............ ...... ............ IF Coefficient of Expansion Coefficient of Water lot Involved Product Table D ............................................... From $obis 8 ............................................ Added Surloctanll ❑ Yes ❑ No Transfer COE to t.kls 25b. Transfer COE to Line 25b. 25. (ate• X (b) C (c) gone" Thai quantity In Coefficient of expansion for Volume change In this lank lull lank its or 17) Involved product per IF A-011'/9yZ 3ZS a .CZ&,So7 Thaisoty7 6 26. (a) Volume change per IF 125 or tab) Oighs per IF in last Volume Change par digit teat Perm. 123) Compul• 1. 4 duramal pisraa. Hctnr tel