COMPLIANCE INFO_1986-2001 - Laserfiche WebLink

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Name of Supplier. Owner or Daalar Addrer No. and Street is) city State Date of Test 15. TANK TO TEST IdeMey by position S_4PER __IJNLEA®&D _ Brand and Grade =I 15a. BRIEF DIAGRAM OF TANK FIELD 1 16. CAPACITY 17. IlL-UP'FQR TEST Stick iiabor Bonen before FIk-up In. . to 14` Gallons s.; 18!' ECIAL:CONDITIONS AND PROCEDURES TO TEST THIS TANK Seeimwkuat eKkena applicable Check below end record procedure In c Nominal Capsule % ®, no U (WtOna By meetseen ate 9 8 r COWRY chat available Gellem T/ in. Tank ❑ Wow M tank ❑ Une(s) bang tested with LVLLT ❑ High wow tie In tank exeavokM inventory maxenunlatloweble lost pressure for all to't' 19. TANK MEASUREMENTS FOR. Four pound rule does not apply to dOublewaoed tanks TSTT ASSEMBLY Complete section below Batons oltank to waft* ............................ � Z M. Add 30" for 'T' probe may ......................... 30 In. I Is four pound rule required' yea U� No ❑ Total tubing to assemble — approximate J_a Z. _, M. The above calculations are to be used for dry soli Conditions to establish a positive pressure advantage, or when laky the fans pound rule to compensate for the presence of subsurface water In the tank Refer to N.F.P.A. 30. Sectlons 2-3.2.4 ane 2-7.2 and the tank manufacturer regarding allowable system teat pressures. From El StelkM ChM 9 Tank ManhdaMufw's ChM ❑ Company Engineering Data ❑ Chale supplied with ❑ Other 2 bight to 12" mark from bottom of lank Gallons 3 Premure at bosom of lank P.5.1. A Pressure at top of tank OFF Depth of bola# �yn� Lr.__�1=�i, P. S. 1. Tank die. Temperature ofSample ................................. (.,_) ......................................... 22. Thermal -Sena reading after circulation Transfer rotes to line 2% Waller table In NOTES The above calculations are to be used for dry soli Conditions to establish a positive pressure advantage, or when laky the fans pound rule to compensate for the presence of subsurface water In the tank Refer to N.F.P.A. 30. Sectlons 2-3.2.4 ane 2-7.2 and the tank manufacturer regarding allowable system teat pressures. From El StelkM ChM 9 Tank ManhdaMufw's ChM ❑ Company Engineering Data ❑ Chale supplied with ❑ Other 20. EXTENSION HOSE SETTING Gallons Tanktopto grade' .................................. in. — P.5.1. Extend no" Of t suctkM tube n" or more OFF below tank top ...................................... 10 In. �yn� Lr.__�1=�i, P. S. 1. •If Fill pipe extend, above graft. use top of 1st. Temperature ofSample ................................. (.,_) ......................................... 22. Thermal -Sena reading after circulation Transfer rotes to line 2% dlpss -73/7 In _ IF 0two iclent of Expansion astoosA 23. Opfts per IF In rape of expected change 327— `•Zin dlpks in COEFFICIENT OF EXPANSION (Complete after circulation) for lnwhred Product 24a. Comechad A.P.O. Gravity M. Observed A.P.I. Gravity ................................... Nydromete employed ................................... M The above calculations are to be used for dry soli Conditions to establish a positive pressure advantage, or when laky the fans pound rule to compensate for the presence of subsurface water In the tank Refer to N.F.P.A. 30. Sectlons 2-3.2.4 ane 2-7.2 and the tank manufacturer regarding allowable system teat pressures. From El StelkM ChM 9 Tank ManhdaMufw's ChM ❑ Company Engineering Data ❑ Chale supplied with ❑ Other 21. VAPOR RECOVERY SYSTEM ❑ Total Gallons Gallons am. iMading RECIPROCAL METHOD 7Ypeof Product ........................................ r(, OFF r{o Temperature In Tank After Circulation ........................................ �J • Z •F Temperature ofSample ................................. (.,_) ......................................... 0-.•F .Z5 - 7.7- Transfer rotes to line 2% 'C'7 21. VAPOR RECOVERY SYSTEM ❑ so" I ❑ sty if 24b. COEFFICIENT OF EXPANSION on Table c a o RECIPROCAL METHOD 7Ypeof Product ........................................ O M+dr~- Employed .................................. 4 -Es" N Temperature In Tank After Circulation ........................................ �J • Z •F Temperature ofSample ................................. (.,_) ......................................... 0-.•F .Z5 - 7.7- WF. From Table A .................................... 'C'7 A.P.I. Grrpsy................................ s ... , . 86 Page a _ L y y • s 2 zz_ Toso quentity M Reciprocal Volume Ch rlge in tug (leaf 17) Mile tank per IF Tranafw to Lkle 211s. 24c. FOR TESTING WITH WATER on Table c a o Observed sanole Tanperoure ......................... •F Corrected A.P.I. Gravity Vftlor Temperature Neer Circulation WF. From Table A .................................... Taft C ...... 0two iclent of Expansion of Water for lnwhred Product TOM, 0 ................................................ FromTable B ............................................ Transfer COE to Llns 25b. Addbd Surfactim7 ❑ Vr ❑ No Transfer CO E to Line 25e. 25. (a) >< (b) _ (C) TOW Wjw" In Coefficient of sages at for Vokmne cleltpe M sale tank hill tank (16 rad 17) I product per •F 26. (a) boa 6 l Z38 7,7-- :9 _ • 0z0Srs 63 Tia !•®2®s-1 Volume change per IF (25 or 24b) Olgft per IF In last Ybkmle change per dips too l J Rape (23) Comgdo to 4 decimal places. Faeroe (a)