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• A TANK TESTING PETRO-TITE TEST RESULTS <br />5630 DISTRICT BLVD, STE 103 <br />BAKERSFIELD,.CA 93313 <br />(8051 397-6555 <br />CUSTOMER WE MOBIL OIL CORPORATION DATE 20 -Aug -87 <br />ADDRESS HAMMER LANE 5 I-5, STOCKTON, CA TANK SIZE 10,000 <br />STATION ID 10-992 PRODUCT SUPER UNLEADED <br />t}tf#tft#tftfitttttff#tfftff#f#ftttfiffif#ftfftit#t#}itf#tttfifi##it##iitfff#i##ttttft#ff##tf#####i}##ftiift#tftf}t##t}}{}} T <br />API GRAVITY 58 VAPOR RECOVERY TYPE <br />TEMPERATURE 76 STAGE I 1 TANK DIAMETER , 95 <br />CORR API GRAVITY 56 STAGE II 0 TANK CAPACITY 10172 <br />t#t#i#fi#ififfttfttftftt#ft#ttt#flit#ii}#ii#ttf#t#fftftfti#f##it####}i##i####it#tiff#fff###tt###tffffft#itf##tfttfffft#ft#f <br />TEMPERATURE/VOLUME FACTOR (a) TO TEST THIS TANK <br />SENSOR READINS: digits 19238 degrees F 81/82 DIGITS PER BERM 312 <br />TANK MWITY 10172 1 COEFFICIENT 0.0005852 EQUALS YOLW CHANGE 5.952654 <br />VOLUME 5.9526544 DIVIDED BY DIGIT 312 EQUALS a FACTOR 0.01907902 <br />a FACTOR FOR THIS TEST 0.0191 <br />_ tuft##fffififff#ti##tit#fi}#ffff###t#}tffffff##fffif#ttfffffffftiiit#if#f#ff#ff#i# fi}iff#itfifftf#i## <br />r . a HYDROSTATIC VOLUME °.:TEMPERATURE s ; !Ei ACCUM <br />PRESSURE Y tc RT (R!E CHANGE <br />CONTROL. <br />.... ` BEfiIN RESTBEFORE AFTER <br />! a -.�xx.-"�•' <_ x,x`c �*:`�a r r � .Z'� � �.�` c. <br />START HIL 1. 43.0 42 250 320 0 070 19243 5 0.096 0.026 <br />2 42 9 42 320 <br />• <br />370 <br />0.050 <br />09243 <br />0 <br />0.000 <br />0.050 <br />3. <br />43.0 <br />42 <br />370 <br />440 <br />0.070 <br />19256 <br />13 <br />0.248 <br />-0.178 <br />4. <br />43.1 <br />42 <br />440 <br />520 <br />0.080 <br />19258 <br />2 <br />0.038 <br />0.042 <br />5. <br />43.1 <br />42 <br />520 <br />600 <br />0.080 <br />19269 <br />11 <br />0.210 <br />-0.130 <br />6. <br />43.0 <br />42 <br />600 <br />670 <br />0.070 <br />19269 <br />0 <br />0.000 <br />0.070 <br />7. <br />43.3 <br />42 <br />670 <br />270 <br />-0.400 <br />19280 <br />it <br />0.210 <br />-0.610 <br />L <br />43.2 <br />42 <br />440 <br />US <br />0.425 <br />19291 <br />It <br />0.210: <br />0.215 <br />10e <br />11. <br />BASE READING <br />12 <br />19291 <br />START L/L 1. <br />13.6 <br />12 <br />20 <br />120 <br />0.100 <br />19291 <br />0 <br />0.000 <br />0.160 <br />2. <br />14.0 <br />12 <br />120 <br />250 <br />0.130 <br />19299 <br />8 <br />0.153 <br />-0.023 <br />-0.023 <br />3. <br />13.9 <br />I2 <br />250 <br />360 <br />0.110 <br />19299 <br />0 <br />0.000 <br />0.110 <br />0.087 <br />4. <br />14.0 <br />12 <br />360 <br />480 <br />0.120 <br />19308 <br />9 <br />0.172 <br />'4.052 <br />0.035 <br />5. <br />13.9 <br />12 <br />480 <br />595 <br />0.115 <br />19315 <br />7 <br />0.134 <br />-0.009 <br />0.016 <br />T -S SER # 1347 <br />BASED ON THE NFPA CODE 329.02 CRITERIA, VE FIND <br />TECHNICIAN...'`}EITHIS SYSTEM TO BE °tIBHT.° <br />��� <br />r CERTIFICATION.# 414811422 <br />",• � _ . ` }.fir �' _ "' � _ P.` � � <br />TEST RESULTS 0.016 <br />