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ARRIVED TEST SiTE®" 1101116 T c,..lOa/A ® '� �" v"' /'c� <br /> i�� PRODUCT <br /> 'HATE/TIME OF FiLL 2 PRODUCT LEVEL AT ARRIVAL. 2-TN®IES RFLOW FILL EVP NOMINAL TANK SiZE 756 <br /> TANK MATERIAL e1 APPROX. AGE YRS. FiLL SIZE/TYPE ! - OVERFILL CONTAINMENT TYPE <br /> VISABLE VENTING APPEARS TO BE AT, r-ILL END, -i' L OPPOSPTP EN IIAS BURP TIME, UNKNOWN, HAS BALL CHECK, OUTER, ! <br /> :ISABLE VAPOR TRAPS TO BE BLED: BALL CMF.CKS, MANNAYS, RETURN LINES RPMOTE FILLS. OTHER. <br /> PIIASE It VAPOR RECOVERY SYSTEM TYPE: BALANCED ASPIRATOR ASSISTED LONG RiR; WELLS MANPFOLDED NONE OnIER <br /> PUMPING SYSTEM: SUCTION TURBINE NAKP. MODEL PIPELINE LEAK DETECTORS Y N A <br /> AFR11ENt NEATiIER CONDITIONS: TEMP. PRETEST POSTEST SUNNY RATNiNG LOUDY NiNDY NIGIT OTHER, <br /> SYSTEM moomreZ/0 mum 0.4 PST DROP 104 II011RS PSI TO BE MAINTAINED ON TANK BOTTOM DURING TEST PERIOD ` . <br /> (IIARTED TANK SiZE "4;5:0 ESTIMATED LINE. GALLONS PRODUCT AnnPD TO FLOTDD SYSTEM TOTAL SYSTEM CAPACITY: 7-5-2 <br /> LIQUID LEVEL CALIBRATIONS " " - TEMPERATURE CALIBRATIONS <br /> PRETEST POS'IEST � <br /> �/ <br /> Lims bk_.LSd 7_4_ JUL ���� - API GRAVITY OF �0 AT � DEGREES F <br /> DFAPI GRAVITY OF a'7p S At /� 60 DEGREES F <br /> IIOVEMF.NT� 37_37 tIiiB IYI Ni L HEALTH COEFFICIENT OF EXPANSION OF . x 00 <br /> AVERAGE J4 j 37 PERMIT/SERVICES <br /> M L 36. 3 ®®® ® C96V 4 .5 Z-/ 76- Z— . 327 Z <br /> QUANT11Y 8 NESCT t VEFIENT L q-tj!DD CONSTANT "A" COEFFICIENT OF EXPARS-1-M X SYSTEM CAPACITY • TEPmE URE CONSTANT "N" <br /> ®a `47 START END GAiN + TIMES LEVET. START END GAIN + TiMES TE PFRATTIRE FINAL <br /> TT)� LEVEL LEVEL LOSS CONS A RESULTS TEMP. TEMP. LOSS CON A RESULTS RESULTS <br /> ® 69 A 6z, ,6/p of 7 <br /> bf <br /> ?�?_ :t/ .� ____ <br /> 70 7/ o <br /> p9 O ,hZ 1.32-7rt COLO 00/Z_ <br /> Monitor Period Standard Deviation •DOL Monitor Period Final Result f <br /> 73- t� 6 196D6 .6l/ *;COS 32-7 -10016- iN? It <br /> . �3t.627 . <br /> S _�.Z. ._�®._.. "�— <br /> 00/Z_ <br /> — - -- --- too/ Z._ '629 ® 64b -app <br /> 9919-r47 -� --- -t 3 —4.54 foo 8 -7 - - <br /> 7 <br /> 6_ .411 9 tw7 <br /> $(g75' <br /> t04 z —' -�----® <br /> CJ/D76 �± .-r f!Uo/Z.. <br /> •111H: r•INAL 11011R or 7r:STING Rrr•),ECTS Ar <br /> _ OS / GAIN o : <br /> WIT(l A STANDARD nrmATION Or:�/_ , OQ <br /> ___.0 <br /> UNNER/OPERATOR 7- 1W31 _S` 46�de4lpelv <br /> 111E HORHPR PZTCIIF.K I TEST METHOD COMPLIES WITH THE STATE OF CALIFORNIA <br /> PERFORi1ANCE STANDARD OF 0.05 CPH FOR TANK iNTEGRiTT TF.STINO. SEC.2 <br /> SITE ADDRESS / CA. CODE OF RF.CS. BASED Upon THiS STANDARD, THE ABOVE RESO/.T F.S NOH <br /> iNI)ICATF. AN UNATNORiZPO RF.LP.A3E EQUAL TO OR GREATER TIiAN 0.05 CPO. <br /> .1YC(RINT <br /> (' INTEGRITY TANK TESTING SYSTEFIS, 166 FRANK NEST CiRCLE <br /> ELEVIF ✓ hh STOCKTON, CA. 95206 ( 9j 466-8036 17 !(800) 261-8318 <br /> TFLEPIiONE ( ) .fes`",/00 CERTIFIED TESTER y !0''l o <br /> SiTE AGENTS_ TEST DATE _-_ rJ �►°' <br /> A <br />