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ARReVED 'FEST SITE-692P7011OURS TANK :AATICN/, PRODUCT <br /> a <br /> DATE/TIME OF FILL`Z DUCT LEVEL AT ARRIVAL INCISES BELOW FILL .dP NOMINAL TANK SIZE <br /> TANK MATERIAL APPROX. AGE Ir-4 YRS. FILL SIZE/TYPE OVERFILL CONTAINMENT TYPE <br /> VISABLE VENTING APPEARS To BE AT: FILL END, FILL OPPOSITE END, HAS BURP TUBE LMKNONN, HAS GALL CHECK, OTHER, <br /> VISABLE VAPOR TRAPS TO BE BLED: BALL CHECKS, NANNAYS. RETURN LINES, REMOTE FILLS, OTHER, <br /> PHASE I/ VAPOR RECOVERY SYSTEM TYPE: BALANCED ASPIRATOR ASSISTED LONG RUN WELLS MANIFOLDED NONE OWER <br /> 2 -• <br /> PUMPING SYSTEM: SUCTION TURBINE MAKE y� MODEL PIPELINE LEAK DETECTORS Y N <br /> MEIENT WEATHER CONDITIONS: TEMP, PRETESTPOSTESt SUNNY RAININr-TLCUPV MINDY .NIGHT OTHER, <br /> SYSTEM FLOODED HOURS 0.4 PSI DROP/01=' HOURS PSI TO BE MAINTAINED ON' ANK BOTTOM DURING TEST PERIOD �s® <br /> CHARTED TANK SIZE./z�® ESTIMATED LINE GALLONS /® PRODUCT ADDED TO FLOOD SYSTEM �I TOTAL SYSTEM CAPACITY: /Z101L <br /> I.IQUID LEVEL CALIBRATIONS TgF1�ERATURB CAL (l, Jj-QHS <br /> PRETEST POSTESTRT1" �E <br /> API GRAVITY OF `�G'' <br /> LINES �7�/ 7�� AT DEGREES F <br /> \° � lW go� A I r <br /> OFJ-0_1, API GRAVITY OF AT 60DEGREESF <br /> MOVEMPNTJ'f f¢ w r COEFFICIENT OF EXPANSION OF, lk <br /> �/ IR �`4a�� <br /> VI Rs i ti. fEAl.TT <br /> AVERAGE <br /> 0 5 s ,000 1 � 1 4949 .f.7 . /Z 4949 S QSz 4 <br /> )DED NE IOVEMENT LIQUID CONSTANT 11A" COEFFICIENT OF BXPAN I X SYSTEN CAPACITY • TEMPERATURE CONSTANT "t <br /> /•�C7o START END GAIN + TIMES LEVEL `" START END GAIN 6 TIMES TEMPERATURE FINAL <br /> 71 PIE LEVEL LEVEL LOSS CONS A RESULTS e�TEMP6 TEMP. IHSS COM A RESULTS ® RESULTS <br /> 40 /o 104909 7Fm .00% ,4w-?w i4v 2s. ti Q/Q! <br /> /J,/o 40 SO -t/6 f -r 004 I�� z 140/0 1949/f <br /> T ® ® <br /> (a0 70 7f1/0 +GtD9 IOD ' .o/0 Z- Q 4 OG/ <br /> (]Q� �f�' /C)+4i�a—f <br /> L M p r oo/00 •Q^��Zj wry- �j -t!0a;®9 <br /> Ito <br /> Monitor Period Standard Deviation V®473 Monitor Per od Final Result <br /> TY3 Sr e23 3 7t/a owl o/4 ®//. <br /> /_d4o .33 43 f/o ao 4116 dye: 4O.Or- 4 <br /> zo <br /> j -�O o <br /> 00.. Oq ZAODZz. ?— + o 9 'coo/ <br /> 106JiP... .�'.f�� r� f// _ �I®Q Alr 2°" ® L o �..Vs✓/v <br /> Oo 0t* Ozz <br /> foo 7 z p oz z ,o io_ _�0-c-Q-' <br /> + 7 foo 6 z z Aw/ X05 tmo�'8 <br /> 40 4d "f j`o0 7 2.... 10" 1030 4tt2l -74.9901 <br /> 4� SS f742n06.3 eoo y a o -.�43_ <br /> N <br /> !7 $ !® ff6/T/ Q 4 &LV a fw 8 00-55 04K/ <br /> THE FINAL HOUR OF TESTING REFLECTS OSS /.GAIN OF: <br /> W ITH A STANDARD DEVIATION OF:+/- ,00 it. <br /> OWNER/OPERATOR T119 ROMER EZTCHER t TEST METHOD WIRLIE8 WITH TUB STATE OF CALIFORNIA <br /> /'� PERFORMANCE STANDARD OF 0.03 GPH FOR TANK INTECRITT TF.STIRO. B <br /> SITE ADDRESS /®�a,00VI V `•- CA. CODE OF RMS. BASED UPON THIS STANDARD, TNB.ABOVB RESULT SNOT <br /> CITY <br /> 146s, .5 G/N G® INDICATE An UWATTIORtZZD RELEASE EQUAL TO i OR CREATBR THAN 0.03 0 <br /> r- �1 INTEGRITY TANK TESTING SYSTEMS, 166 FRANK WEST CIRCLE <br /> COUNTY L> V GSTOCKTUN, CA. 95206 (209) 66.8036 ®(800) 262-8378 <br /> TELEPHONE ( )( *4z, —//ob CERTIFIED TESTER <br /> .J <br /> SITE AGENTS I Ci/� _ TEST DATE ` 7 <br />