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ARRIVED TEST SITE 7d ,30 HOURS TANK TION/B MVy If�16/��•C�7��a]LVopRODUCT <br /> DATE/TIME OF FILL PROWCF LEVEL AT <br /> AT ARRIVAL�IN0IES BELOOWW FILL TOP (NOMINAL TANK SIZE yy- ID Cem D <br /> TANK MATERIAL —APPROX. ACE �^'R- yp5. FILL SI2E/TYPE I OVERFILL CONTAINMENT TYPE <br /> VISABLEIVENTING APPEARS TO BE AT: FILL END, FILL OPPOSITE END HAS BURP 'PURE, UNKNOWN, ,IIAS BALL OIECK, OTHER, <br /> VISABLE VAPOR TRAPS TO BE BLED: BALL OIECKS, MANWAYS. RETURN LINES, REMOTE FILLS, pOTIER,'. <br /> PHASE 11 VAPOR RECOVERY SYSTEM TYPE: BALANCEDPIRATOR SI 7E0 (LONG RUIN WELLS , NANI FOLDED OTIIE0. <br /> .PUMPING SYSTEM: SULTIOY .TURBT MAKE��QQ MIODEL //•.N�- PIPELINE LEAK DETECTORS Y)N NA <br /> AMBIENT MEATIER//�C��1ONNDDITIONS: TEMP. PRETEST6]LPOSTEST� UNNY RAINING 1,0110 WINDY IOIT OTHER, L� <br /> SYSTEM FLOODED TIOURSo 0 0.4 PSI DROP `0_ HOURS PSI TO BE MAINTAINED ON TANK BOTTOM DURING TEST PERIOD /o <br /> OIARTED TANK SIZED-- LO,,n n e ESTIMATED LINE GALLONS <br /> PRODUCT ADDED TO FLOOD SYSTEM�70TAL SYSTEM CAPACITY: 1�n�1, �7 <br /> LIQUID LEVEL CALIBRATIONS <br /> PPR/E�TEST POSTEST TEMPERATURE CALIBRATIONS <br /> LINES M�0 /Y 70 %�/�� 0 7� <br /> —C((2 ,WXAPI GRAVITY OF AT 74 <br /> 9 73, ' DEGREES P <br /> OF 3�J�' ya x/ ,33, <br /> p� .may API GRAVITY OF 3t,y AT 60 DEGREES F <br /> MKIVEMD:N _✓1,L 3fi �A O o o Ng <br /> COEFFICIENT OF EXPANSION Wiy..– .�eeISY6SF•1(v9 <br /> AVERAGE 3�_4 34 y/ - o00YS8' /9/eo7 5.`/99 <br /> QUAN00/377 �1.- ocojz /a�eo .7 <br /> (]TI�T`Y/ADDE NEL( 5 MOVEMENT' LIQUID CONSTANT "A" ; COEFFICIENT OF E% ANSiON K SYSTEM CAPACITY TEMPERATURE [DISTANT <br /> OJVJ START ENO GAIN • TIMES LEVEL START END GAIN s TIRES TEMPERATURE FINAL <br /> fl—ME LEVEL LEVEL LOSS CONS A RESULTS TEMP. TEMP. LOSS CON A RESULTS RESULTS <br /> 095 <br /> 61 V7 <br /> 1t9ff-33Z'-y 3 /y ii/f/•1-,.0 O0OO.OOJ`Y1yYHy' i1!/'yi'I ..y.•.�'owG0vas55ss.��i 7 ,.o0icoG �+.:..6.apove'o-6 <br /> eo'llll <br /> oew�o <br /> IdIl7 Xt <br /> a <br /> � - .OS oo 7 WOS y •s.YS+t+}-oO$�0o4&'' As6'Sl J <br /> '�;Fr',ocooOOo0aOoOO O�13y1,�33o`o( P0 <br /> 1!t voy3 <br /> 91 <br /> 137 eols 7 + 005 <br /> y :! ' 0 3 <br /> oO3 , 'A7 <br /> �9 6_ 00 c' ao <br /> o-3 o r00Q ' <br /> o0 <br /> o- <br /> i <br /> .o- <br /> / 65 <br /> //7 d 3 .3 -f�,�r)DYZ <br /> a T/ bl�o7 off— <br /> Is <br /> ' <br /> 0 o ' d <br /> t_ I .05- GAS , " 8' oo/'{ <br /> `rr 3 , o oLPi , o 0 o S <br /> THE FINAL HOUR OF TESTING REFLECTS A LOSS / GAIN F: Q� y <br /> WITH A STANDARD DEVIATION OF: ♦/- <br /> OWNER/OPERATOR RNER EZY 0' <br /> 1EKHII METHOD OF PRECISION TESTING T11E RESULTS, <br /> ARE WITHIN ARE NOT WITN THE STATE OF CALIFORNIA AND THE NFPA 329 <br /> $ITE ADDRESS1 OF A MARIMIM LOSS/GAIN OF .05 GALLONS PER ONE IHGUR OF <br /> /CITY , sT0 TESTING FOR A TANK SYSTEM TO BE CONSIDERED TIOIT. <br /> COUNTY F INTEGRITY TANK TESTING SYSTEMS, INC. 166 FRANK NEST CIRCLE <br /> S70CKTONo CA. 95206 09) / B 3 (800) 2662-8378 <br /> TELEMKTNE (�J 9 0o a CERTIFIED TESTERS <br /> SITE AGENTS ��--[% TEST DATE /O ' / V <br />