COMPLIANCE INFO_1986-1997 - Laserfiche WebLink

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N" 14. L I., .. : Nome of slowler, Owner of Dealer •�:fdfsoll No and Street 11) City tn-. slaw Dole of Test :r"., 15. TANK TO TEST 38. NET VOLUME 0J"NS EACH W�WG 15a. BRIEF DIAGRAM OF TANK FIELD '16.?CAPACITY From 29. Reading ntNominal 32. Product in Graduate 33. Product Replaced cc) station Chart 0- ❑ Tank Momileclurer's 37 Computation (c) - (a)• Expansion • Contraction - Idereft by "I- At Low Level compute Change W Hour INFPA criteria) Volume Minus Expansion (-) or Contraction H Inv) 4711) Capacity Chart Gallons ❑ pany Engineering Data VfZho-ne Level to which Restated 0111144111`11 fit"" 'After - Reading Product Recovered I-) TIME•of I bt 24 j supplied with cvt farfame and Grade By most accurate capacity chart available 13 Other Gallons 17. FILL -UP FOR TEST Total Gallons "Iwo sa. Flooding in. Inventory low, Gallons Tank Diameter 74h 18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK ❑ water In lank El Uns4s) being Wed with LVLLT and record 'procedtirsinlop (27). ❑ High water table In lank excavation Like moxismate allownwo we pressurs, for so tests. 19.- TANK MEASUREMENTS FOR 41� Transfer total to line 25a Few pound ruts does not apply to doublewallod tanks. Conaplets, sectilom below: TSTT ASSEMBLY 21. VAPOR RECOVERY SYSTEM ❑ step I 0smoo if &Mom of lank to grade* ............................ M. 30 Add 30" for 'r probe way ........................... In. 24b. COEFFICIENT OF EXPANSION 44 ib 1. is low III two mq"k�, Yes ❑0 No Q Total tubing to segambis approximate ... .......... In. RECIPROCAL METHOD Type Product ,f. )*it$* in Ir mark tom 604wn of tank 20. EXTENSION HOSE SETTING In. Of ............................ R•., •In. Tank top to grade .................................. Hydrometer Employed ..................... ysq "T Extend hoss, on auction tube It" of more Temperature In Tank S. Pressure at bottom of tonk, P.&L below tank top ...................................... In. 'if W After Circulation ................................. Temperature of Samoa ............... ............... IF OL'Prissours; at tap of bank Fill pipe extends above grade. use too of 22. Thermal -Sensor reading aver CkMlmiw Difference W-) .................................. IF 77! Depth of burial In. F train 23. Digits per IF in •range of expected skentile digits In. Observed A.P.I. Gravity ............................ ftQcipro"-2-4- Page Die nk Ta COEFFICIENT OF EXPANSION (Complete after circulation) . + ozu . . ... . .......... 24a. Corrected A.P.l. Gravity a Taal quantity In Flociprocei volume change In Uk IF 4 Water few in. Observed A.P.I. Gravity ................................... fuel (16 or 17) Oft lank per Transfer to Line 2$L That above cialcullationts we to be used for dry Boll conditions to edsbfthapook*oproomma&antsio.orwhon using the four pound rule to w" for Vid, presence of subsurface water in the tank PAW to KFPA. 306 Sections 11-3.14 and 2-7.2 and the to(ost ansinufflackars" NOW" &NOW" "In'ta'" lost Rroaau'es. r. 14, Hydrometer employed ...................... - H Observed Sample Temperature ................. 24c. FOR TESTING WITH WATER seeTable C&O Corroded A.P.I. Gravity Water Temperature after Circulation @ GVF. From Table A .................................... Table C .......................... ............. ....... IF Coefficient of Expansion Coefficient of WSW for Involved Product Table D ................................................ FromTable 8 ............................................ Transfer COE to Line 25b. Added Surflictent? E) Yes 0 No Transfer COE to Lim 25b. 25. (a) r (b) a (C) gallons Total quantity in Coefficient of expansion for Volume change In this lank full tank ( If or 17) Involved product per IF 26 (a) jL4LA(* 2D L) �1!525 A This is . 019#8 per IF In Ised _,f.V" angs par dW 11 "Inkno!" 5two W- IP 9F TUT FROMOM 30. wmosTAnc PRESSURE CONTROL VOLUME MEASUREMENTS (V) RECORD TO.101 GAL. 34. TEMPERATURE COMPENSATION USE FACTOR W 38. NET VOLUME 0J"NS EACH W�WG 39. ACCUMULAIiD CiAW4,:` '41C 28. - DA P 4OWd details of Setthlo Up and rutining tat (Use full wnp of Un N needed.) 29. Reading Standpips Level In Inches 32. Product in Graduate 33. Product Replaced 35. Thermal Sensor Reading 36. Change Higher • Lower - 40 37 Computation (c) - (a)• Expansion • Contraction - Temperature, Adjustment At Low Level compute Change W Hour INFPA criteria) Volume Minus Expansion (-) or Contraction H Inv) 4711) seg Ming Reading Level to which Restated 0111144111`11 fit"" 'After - Reading Product Recovered I-) TIME•of I bt 24 j cvt .CIA4 74h 44 ib i 77! + ozu I&E0 12'su I'Ll"Zilo -�Oub hlm q 4 z4 v 9 (-4(-) -T L + 1116T.Tank 1111114111 Data Chan Adtional Info a on 1 Not, Volume Change 0 of al Signature of To"& PNUU e. . . I L 1111stsiment: ft Tank and product hancilling System has been tostifif light according to the Precision Test Criteria as established by N.F.P.A. publication 329. This Is not Intended to Indicate parmission'tof a. leak. OR 0 Tank and product handling system has failed the tank tightness test according to the Precision Tog Criteria as established by N.F.P.A. pubikaticiii 329. It Is the responsibility ol'the owner and/or operator of this system to immediately advise state and local authorities of any. Implied hazard and the possibility of any reportable pollution to the environment as a result of the Indicated failure of this' system. Heath Consultants Incorporated does not assume any responsibility or liability for any Was of product to the environment. I C1 Tank Owner/Operator V..c -- Oato