COMPLIANCE INFO_1987-1995 - Laserfiche WebLink

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� I Name of Supplier, Owner or Dealer Address No. a 15. TANK TO TEST lipf 3 15a.'BRIEF DI Identify by position L Brand and Grade 17. FILL -UP FOR TEST Stick water Bottom before FIII-u P In. Z to In. Tank Diameter -16. CAPACITY N71n at Capacity 21.bo 0 of Product .................. t ...... .............. Gallons By most accurate -7 capacity chaff available — H Temperature In Tank Gallons After Circulation ........................ ..... . &71 IF 18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK 11 W.I., In tank 0 Llne(s) being tested with LVLLT See manual sectionsapplicable. Check below and record procedure In log (27). El High water table In lank excavation the Maximum allow* able test pressure for all tests. Four pound rule does not apply to doublewalled tank*. 19. TANK MEASUREMENTS FOR TETT ASSEMBLY Complete section below: Bottom of tank to grade' ............... Add 30" for "T' probe easy ........................... 30 In. 1. Is four pound rule required? yes❑ No [�' I Total tubing to assemble - approximate .......... 2. Height to I r mark from grade In. 20. EXTENSION HOSE SETTING Tank top to grade* ..... j .............. In. • 3. Pressure at bottom of tank P.S.I. Extend hose on auction tube 61 or more below tank top ...................................... 4. Pressure at top of tank P.S.I. 'it Fill pips extends above grade, use top of fill. USE WITH THERMAL SENSOR Depth of burial In. PN5039 (Blue Box) 22. Thermal -Sensor reading after circulation 6, 1 -7 a Tank die. Z' In. digits IF Between .0( 23. Digits per IF In range Of expected change I 00 0 t -star table to lank bottom In. NOTES: digits 24a. IF USING THERMAL SENSOR DTS-2000 OR OC -2000 WHICH READ 1000 DIGITS PER OF TRANSFER 1000 TO LINE 26, DIGITS PER OF IN TEST RANGE. The above calculations are to be Used for dry $oil conditions to establish a positive pressure advantage, orwhon using the four pound rule to compensate for the presence of subsurface water In the tank ores. I C Cn PU P cr_ < win sow :°C%j C/3 C.D Vale of 1051 From Station Chart Tank Manufacturer's Chart 0 Company Enginoring Data 0 Charts supplied with Tank Teelar 0 Other Inventory In Tank, Water Bottom Top oil equipment Total Ouantity Total Gallons so. Reading 21, VAPOR RECOVERY SYSTEM . 0 stop 1 171 stage if 24b. COEFFICIENT OF EXPANSION RECIPROCAL METHOD. 'type of Product .................. t ...... .............. -7 Hydrometer Employed ...... .. ............................ — H Temperature In Tank After Circulation ........................ ..... . &71 IF Temperature of Sample ................................. (061�IF Difference (+/-) ......................................... IF Observed A.P.I. Gravity ................................. -<L I Reciprocal Page N W9 Total quantity In Reciprocal Volume change In full tank (17) this lank per IF Transfer to Line 26s. 24c. FOR TESTING WITH WATER.so Tabs c&D Water Temperature after Circulation ', I,) Table C from Thermal Sensor ............................ _*F Coefficient of Water Table D .................... I ........ ................ Added Surfactant? 11 Yoe 0 No Transfer COE to Line 25b Rate, to N.F.P.A. X Sections 2-3.2.4 and 2-7.2 and the tank 26. (a) P)A- X M manufacturer regarding allowable system lost pressures. gallons Total quantity in Coefficient of expansion for full lank t171 I , Volume change In this tank VIVO— product per IF 26. 7 �5& L/ ?S- 1000 = oo tib/73S%' Volume change per IF (26 or 24b) Digits Per IF In test Volume rtrw-n ny 0,1f ,