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*A Q A TANK TESTING <br />5630 DISTRICT BLVD., SUITE 103 <br />BAKERSFIELD, CALIFORNIA 93313 <br />TANK OWNER'S NAME <br />MOBIL OIL <br />CORPORATION <br />DATE OF TEST 27 -Jul -88 <br />ADDRESS OF TANK <br />3202 W. HAMMER LANE, STOCKTON, CA <br />PRODUCT IN TANK UNLEADED <br />MAR .2 <br />LOC \ STN ID <br />10-992 <br />NOMINAL CAPACITY 10000 <br />ffftfffffff4tfffffftfttffftfffff4tfftttfffftffff4fttffffffffftfttffffffftftfftffm <br />afffffffffffffff+ftlfffiffffffffftt+ffffffifffff <br />TYPE OF PRODUCT <br />GASOLINE <br />THERMAL SENSOR 801 READING <br />19635 <br />TANK`-DIAMET 9: <br />TOTAL TANK QUANTITY <br />9,758 <br />TEMPERATURE BETWEEN <br />(IN F) <br />82/83 <br />OBSERVED A?I GRAVITY <br />56 <br />DIGITS PER DEGREE IN <br />RA16E <br />SAMPLE TEMP. (IN F) <br />84 <br />OF EXPECTED CHANGE <br />308 <br />}fftttttf4i4ftfffft+fffftfffffft{ffffftf}fffffffff}f}}f{ffffffffftft}fftttffftff+ff}ftfftfff}+ttftf}ffffftftff}+f+t4ffffffftffffffft <br />TEMP. IN TANK AFTER CIRCULATION <br />(IN <br />F) 82.4 <br />DIFFERENCE 2 <br />R E C I P R O C A L <br />1514 <br />PAGE NUMBER <br />60 . <br />TANK QUANTITY 9,758 <br />DIVIDED BY RECIPROCAL 1514 <br />= COEFFICIENT OF EXPANSION <br />6.445178 <br />COEFF. OF ENIPANSION <br />6.445178 <br />DIVIDED BY 016ITS 308 <br />= A FACTOR FOR THIS TEST <br />0.0209 <br />tftff4f4fffttffttffttfftfffffttftttftfftft4f+fff4t4fttfttftffftfffffffffff{fff{ffff}ttf}}}}{}tfffffffffffffffttfftffttffit4+fff+tfff <br />fffttffftttifffftfftttffftftiiifitt+fttttftfttftfttffffffffittitftttftttffft}t}}{f}{}fftftffftffttffffftfftfftffffff{ff{{}tfff+ffffff <br />HYDROSTATIC <br />VOLUME <br />TEMPERATURE <br />NET ACCUP.. <br />PRESSURE <br />MEASUREMENT <br />COMPENSATION <br />VOLUME CHANGE <br />CONTROL <br />CHANGE <br />ftf{ftitftfif}{}}}f{ffftffitffffffitiiiiftffftffttttfttftfftftfttfftttfttfftffftftftffftttffftfttfifftifftttftfiffifiitftftfifffftf+, <br />VOLUME <br />THERMAL <br />REPLACED - <br />SENSOR <br />BE61M <br />RESTORED <br />BEFORE AFTER RECOVERED <br />+ READING CHANGE <br />CORP. <br />TEMP AN <br />BASE REASIN <br />42 ' <br />19635 <br />START N/L 1. 43.1 <br />42 <br />230 300 0.070 <br />19635 0 <br />0.000 <br />0.070 <br />2. 43.2 <br />42 <br />300 380 0.060 <br />19637 2 <br />0.042 <br />0.038 <br />3. 42.9 <br />42 <br />380 435 0.055 <br />19648 11 <br />0.230 <br />-0.175 <br />4. 41.2 <br />42 <br />435 395 -0.040 <br />19648 0 <br />0.000 <br />-0.040 <br />5. 43.4 <br />42 <br />395 485 0.090 <br />19652 4 <br />0.084 <br />0.006 <br />6. 43.0 <br />42 <br />.485 550 0.065 <br />19656 4 <br />0.084 <br />-0.019 <br />7. 43.1 <br />42 <br />550 630 0.080 <br />19663 7 <br />0.146 <br />-0.066 <br />8. 43.1 <br />42 <br />630 700 0.070 <br />19667 4 <br />0.084 <br />-0.014 <br />9. <br />10. <br />11. <br />12. <br />BASE READIN <br />12.0 <br />1%67 <br />START L/L 1. 14.2 <br />12.0 <br />25 165 0.140 <br />19671 4 <br />0.084 <br />0.056 <br />2. 13.8 <br />12.0 <br />165 273 0.110 <br />19677 6 <br />0.125 <br />-0.015 <br />3. 13.8 <br />12.0 <br />275 385 0.110 <br />19682 5 <br />0.105 <br />0.005 -01010 <br />4. 13.8 <br />12.0 <br />385 495 0.110 <br />19688 6 <br />0.125 <br />-0.015 -0.0A5 <br />5. 13.8 <br />12.0 <br />495 605 0.110 <br />19693 5 <br />0.105 <br />0.005 -0.020 <br />TECHNICIANI M' 4TS <br />THE TIME OF TEST, THIS SYSTEM <br />���� N F P A REQUIREMENTS FOR A <br />CERTIFICATION 414811422 TIGHT SYSTEM. <br />NUMBER <br />THERMAL SENOR <br />SERIAL NUN1ER 1346 <br />TEST RESULTS -0.0_) <br />