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"FCEIVED JUL 1' 4 <br /> n 1987 <br /> • Venting: FE(SVUkn PUMP:-&P A�FIILL:�" TANK LOCA-ION:�.J dS: O� � "4Z-,1:1 .f( C{+-a� SA1`Tjw PRODUCT <br /> REMLUU:S: 1fc31.A'Taa (�-+ /-1LL �,p <br /> LIQUID LEVEL CALIBRATIONS TOP OF FP TO BIN OF NK). <br /> PRETEST POSTE-ST <br /> TOP OF FP TO TOP OF NK 33 <br /> LI.NES j JD _ Sl_ /C <br /> TANK DIAMETER g_L <br /> OF �!6 y,! va 3 D _ <br /> H2O PRETEST'-POSTEST -t!5- <br /> MOVEMEVr 37 -;G 7d� a�. TEMPEPEBATURDI-CALIARAZONS <br /> AVERAGE INCHES ATT TEST START 57" API PRODUCT GRAVITY.;L•l?AT B F. • GRAVITY 3 y AT 60 F. <br /> VS — p7.a 00185iP o0o VS-7-; 8,ooh ? 6 Y7l <br /> LIQ QUAN ADDED - LINE MDVMATT • LIQ CONSTANT (A) COEFFICIENT OF EXPANSION X TANK CAP. GALLONS TEMP. CONSTANT (B) <br /> I <br /> 2900Ari LEVEL LEVEL GAIN=+ TIMES - LEVEL TEMP . TEMP . GAIN + TIMES - TEMP . FINAL <br /> TIME START END LOSS — CONS A - RESULT START END LOSS — CONS B=RESULT RESULTS <br /> F- o3a3 76D , 00 3 , G6 + 0036 — 0.3X96 <br /> -7 1- 6— 1 - -7 033 fko 4rooj ,o o.3G6 _ o 0 96/ <br /> CJ dt 6 f I Sb' I I o133 , gS l 7 S� I:ov l I 0 0366 00 9G <br /> /6% -S-)/ -1< 0076 95-S , ST i. oa3 a /o9d' ? o A� <br /> o03 0/os� - o 0o a <br /> ��o .0 0-21jL o0-1le <br /> p,r '13 33 - S I II ;"ooy� , y5-w SY9 �. 00 - aos?66 vvsa' t <br /> 3 Y 133 '� 00/9 1 00 . S Y9 . `! y� .-oo j 3. 66 0 0 s g <br /> OW';ER/OPERATOR �OGC7 S>'F/GSC USING THE HORNE Y CHEK METHOD THE p <br /> SITE ADDRESS �OO 4J L'. A.{jiJ ry.� �>n2 LAA/l� TEST REFLE ALO' /GAIN PER NOUR OF: FINAL HOUR = p / a0 JS <br /> THE RESULTS• ZZ W-:".?ir APE NOT �'_7"'ETT THE NFPA <br /> C:l'..Si'OCKioJ CO.,NTY S .T:' 329 GUIDELI! t -A-TZIMUM LOSS OF .05 GALLONS PER. <br /> PER ONE HOUR FOR A TIGHT, TANK / SYSTEM. <br /> TELEPHUSE ( ) <br /> DATE OF PRECISION ;TS".'ING <br /> AG=.\T0,4gy SAkrAe1,✓6 <br /> INTEGRITY TANK 'ES-NG SYSTEMS, INCORPORATED <br /> 166 FRANK WEST CIRCLE, STOCLTON, CA. 95206 <br /> (209) 666-8036 1 800 2622�-8378 <br /> TEST TECHNICIAN <br />