COMPLIANCE INFO_1986-2001 - Laserfiche WebLink

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Name o' Suppher. Owner or Dealer -- 15. TANK TO TEST Gallons Sea manuaf sections applicable. Check below and record procedure In log 127). + - Identity by position Line maximum allowable test pressure for all tests tour pound rule does nor apply to doublewaned tanks . 19TANK MEASUREMENTS FOR A M Brand and Grade TSTT ASSEMBLY {-10 _ V� _j_8 c 17. FILL -UP FOR TEST '�-- ❑ Stage 1 ❑ Stage if -, Stick. Wafer Bonom before Fill -up --_� In to 4" Address No. and Straalft) City Stats 15a. BRIEF DIAGRAM OF TANK FIELD 16. CAPACITY Nominal Capacity /O� C>Q 0 Gallons Gallons 1 In. Tank Olnrtn•ter By moat accurate yg capacity chart available Gallon• Inventory • of burial _ ! __ M din r • in table .._ In. NOTES: The above CeleulaIIOMI are to be used for dry moll condltlone to establish a poettwe pressure advantage. or when using the lour pound rule to compensate for the presence of subsurhace water In the tank Mea Refer to N.F.P.A. 30. Sections 242.1 and 2-7.2 and the tank manufacturer regarding allowable system test pressures. V IF 23. 019ks per IF In range of expected change ___25;Ik— digks COEFFICIENT OF EXPANSION (Complete after circulation) 24a. Corrected AP.1. Gravity Observed AR 1. Gravity ................................... _ Hydrometer employed ................................... H Observed Sample Tenpereure ......................... •F Corrected A.P.I. Gravity ® OWF. Fran Table A .................................... ---. - Coefficient of Expansion for Involved Product From Table ! ........................................... - - Transfer COS to Line tab. Dale of Test From ❑ Station Chert ® Tank Manufacturer's Chart ❑ Company Engineering Data ❑ Chafe supplied with ❑ Other 18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK ❑ Water In Mk ❑ Line(it) being tested with LVLLT Gallons Sea manuaf sections applicable. Check below and record procedure In log 127). ❑ High water table In tank excavation 614 IF Line maximum allowable test pressure for all tests tour pound rule does nor apply to doublewaned tanks . 19TANK MEASUREMENTS FOR A M TSTT ASSEMBLY {-10 _ V� _j_8 Complete lection below . 0 Big,� Volume change In this tank per IF 21. VAPOR RECOVERY SYSTEM ❑ Stage 1 ❑ Stage if ! 3d Bosof tank to graft* ............................ in • Add 30" for 'T probe any ........................... 30 M. Compute to 4 decimal places. I Is four pound rule repurre417 yea NO ❑ Tau mbing to resemble - approximate ............. In. /5 20. EXTENSION HOSE SETTING 2 1Mrght to t2" mark from bottom of tank M 47 Tank top to grade* .................................. M. Extend hose oil auction tube a" or more 3 Pressure N bottom of tankP S. t� / O below tank top ...................................... In. Q a Pressure al top or tank /' h / 4 p S f - - - - -1 'H Fill pipe extends above grade. use top of tilt. t 22. Thnnnal•Sansor reading atter circulation -- _ • of burial _ ! __ M din r • in table .._ In. NOTES: The above CeleulaIIOMI are to be used for dry moll condltlone to establish a poettwe pressure advantage. or when using the lour pound rule to compensate for the presence of subsurhace water In the tank Mea Refer to N.F.P.A. 30. Sections 242.1 and 2-7.2 and the tank manufacturer regarding allowable system test pressures. V IF 23. 019ks per IF In range of expected change ___25;Ik— digks COEFFICIENT OF EXPANSION (Complete after circulation) 24a. Corrected AP.1. Gravity Observed AR 1. Gravity ................................... _ Hydrometer employed ................................... H Observed Sample Tenpereure ......................... •F Corrected A.P.I. Gravity ® OWF. Fran Table A .................................... ---. - Coefficient of Expansion for Involved Product From Table ! ........................................... - - Transfer COS to Line tab. Dale of Test From ❑ Station Chert ® Tank Manufacturer's Chart ❑ Company Engineering Data ❑ Chafe supplied with ❑ Other 24b. COEFFICIENT OF EXPANSION Total Gallemi Gallons N. Rending Temperature In Tank Aft« Grculstion ........................................ ....................... 614 IF 7-610 0 EP- I= / 0 A M Rw4wocat//%"� P., a _140— {-10 _ V� _j_8 Tranaler total to line 2a• . 0 Big,� Volume change In this tank per IF 21. VAPOR RECOVERY SYSTEM ❑ Stage 1 ❑ Stage if 24b. COEFFICIENT OF EXPANSION x (b) RECIPROCAL METHOD T"M a product ........................................ Hydrometer Employed ................................. i - / E H Temperature In Tank Aft« Grculstion ........................................ ....................... 614 IF Temperature of Semple ................................. �N Observed A IDA. Gravity ................................. Rw4wocat//%"� P., a _140— _ Z / . Toed quantity M Mdprooei full tank (icor 17) . 0 Big,� Volume change In this tank per IF Volume change per IF (25 or tab) Transfer to Lina Zan. Volume Change per digR 24c. FOR TESTING WITH WATER •en Table C A D View Temperature atter Circulation TableC ................................................ IF Coefficient of wow Table0 ................................................ Added aurt.,.l ❑ Vas ❑ No Transfer COE to Line tab. 25. (a) Total queltity M x (b) _ O gallons Coefficient of expansion for Volume change In this lank full tank (ill or 17) Involved product per IF 26. (a)�,g3 Q 3 ip _ _ Z = 1 0 Z(j 0 7 5� \ The 19 Volume change per IF (25 or tab) Dlglfe per IF In tit Volume Change per digR tat J Rape 123) Compute to 4 decimal places. factor (a)