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ARRIVED TEST SITE b735HOURS TANK LOrATION/A ") ; a/.s~�T _PRODUCT /4tvry--e- O/L' <br /> DATE/TU@ -712-9 OF FILL :2-*4'44 PRS. „T LEVEL <br /> LLAT ARRIVAL '21INOIES BELOW FILL TO, NOMINAL TANK SIZE <br /> TANK MATERIAL APf <br /> PROX. AGE—L4—YRS. FILL SIZE/TYPE 4 OVERFILL CONTAINMENT TYPE <br /> VISABLE VENTING APPEARS TO Be AT: F1 LL END PILL OPPOSITE END, HAS BURP TUBE, LINKNOWN,.. HAS BALL CHECK, OTHER, <br /> VISABLE VAPOR TRAPS TO BE BLED: BALL CHECKS, MANWAYS, RETURN LINES, REMOTE PILLSI OTHER, - --� <br /> PHASE 11 VAPOR RECOVERY SYSTEM TYPE: BALANCED ASPIRATOR ASSISTED I'/LUNG RUN WELLS MANIFOLDED NONE (TIER <br /> PUMPING SYSTEM: SUCf10N TURBINE MAKE e4/'Q OQZ>�a4Tc-�IODEt+NC.D�N PIPELINE LEAK DETECTORS Y N NA <br /> AMBIENT WEATHER CONDITIONS: TEMP. PRETEST6_[POST,ES/T 9d - � RAINING CLOUDY WINDY NIGHT OTHER, <br /> SYSTEM FLOODED '93 0.4 PSI DROP �11A 1100RS PSI TO BE MAINTAINED ON 'TANK BOTTOM DURING TEST PERIOD <br /> CHARTED TANK SIZE 73 L S ESTIMATED LINE GALLONS S PRODUCT ADDED TO FLOOD�SYSTEM�TOTAL SYSTEM CAPACITY:-73 73 <br /> 1 <br /> LIQUID LEVEL CALIBRATIONS TEMPERATURE CALIBRATIONS <br /> PREE/T�EST POSTEST <br /> LINES Sl- p✓ __1 ___ API GRAVITY OF O • AT DEGREES F <br /> OF 3/ 3/ API GRAVITY OF�AT 60 DEGREES F <br /> IUVEHEN7tG COEFFICIENT OF EXPANSION OF <br /> AVERAGE 3 - 43,4 - . . 3 3 3 �L <br /> ANT _ <br /> Itlw INES FIOVEFIENT LIQUID CONSTANT COEFFICIENT OF EXPANSION X SYSTEM CAPACITY . TEMPERATURE CONSTANT "B" <br /> START END GAIN • TIMES LEVEL START END GAIN • TIMES TEMPERATORE FINAL <br /> TIME LEVEL LEVEL LOSS CONS A RESULTS TEMP. TEMP. LOSS CON A RESULTS RESULTS <br /> O02—64 15 Z -Z.5 .am5 - -0,012.5 .77/ .770 .dam .ab ,003L7 A4107p2- <br /> O 62- 60 - L -.00 770 70 e .00 // <br /> G 4 -Z'S -.00/zS .770 77o zs .DO! 2-5' <br /> 09z' 4,5 —00zz5 A 1770 6 .00/ -,cb3a 1e0/4)7- <br /> 9zy 67 6¢ _,3 --,00/S 769 79 oo/ <br /> z 6 7 6P ,00/ ,0032.7 ¢ 0c7/7 <br /> L/. S 3 - o0/S 7Zr 74f z5 <br /> 44. /./, 5 57,5 --4 civ Z_ 7AW .767 ,cw/ : -„0,0377 frzyz7 <br /> ca/s- 767 ,1 .7(.7 Ts; Cr- T4 <br /> S _ 6 .'S ,58 3.5 -,00/75 7C7 . 76L .00 -eif)32- 4:00/5' <br /> Z O ,L 00/ <br /> —,ck-JZS 764 S O -2-7 f,00677 <br /> 0/4 -3 -IOd/S 6 ,7fsS 10 r>- ,00/5- <br /> Ip b - 4 _ -.002 765 z9 _j2i7 <br /> -' 00z <br /> 1.6 /. oc! 74 7L4 ->�/ 4e11400Gz. <br /> 103 - .� -� .Do 2— rA , 002„ <br /> fig $ S 60 -3 - Fa0/7 f' 76 .00175OouS -¢ fau'0z <br /> So 63 5.5• - -,o ,62- ,N�/ - c 00673,3, -,vD/7 7G2 7Lz 00/75 <br /> 'HIE FINAL HOUR OF TESTING REFLECTS LOS / GAIN OF: <br /> WITH A STANDARD DEVIATION OF: +/- jW <br /> OWNER/OPERATOR /R`��'�CT /�A�`^� •`�Q�•�--•Q51NG THF. HORNER EZY CHEK I METHOD OF PRECISION TESTING THE RESULTS, <br /> ARE WITHIN /SITE ADDRESS S�Zr� ” r/f��l� �r� GUIDELINES OF A MAx M� S/iGAINTor.OS GALLONS PER ONE r CALIFORNIA AND THOURFOF PA SZ9 <br /> m <br /> S/ DG v�OBJ TESTING FOR A TANK SYSTEM TO BE CONSIDERED TIGHT. <br /> COUNTY ) _^TO���� INTEGRITY TANK TESTING SYST a6, INC. 166 FRANK WEST CIRCLE <br /> d>r�`� V STOCKTON, CA. 95206/' ( 9) 466-8036 (800) 262-8378 <br /> TELEPHONE (? ) 1743 • <&Av o, CERTIFIED TESTER l Cz. ;. p01- `fid &3� ' <br /> SITE AGENTTEST DATE_ 8 L 9 f$O <br />