Laserfiche WebLink
• Ainlay Tank ' Tegrity Teler <br /> REPORT Date 8-31 -89 <br /> Company BOBCAT CENTRAL Address 1113 Shaw Rd , Stockton , CA <br /> Brand Name Exxon Grade of Product Unleaded Re u ar <br /> Gallons 2002 API Gravity 56 . 7 Coefficient of Expansion . 00066569 <br /> Coefficient of expansion x gallons = Factor to be used in this test fori,each 59 . 5 <br /> degree of temperature shift 82b <br /> Factor 1 . 3325312 <br /> Test #1 <br /> Thermometer Net Change <br /> Shift due to Temperature shift - . 0396 <br /> Start End + or - Temp. only Times Factor, - •0527682 <br /> Time 11 :47 12 : 47 Temperature shift times <br /> #1 Top 81 . 6069 81 . 5938 x 25% factor equals volume <br /> change due only to <br /> #2 Mid. 80 . 3605 80 . 3342 x 50% Temperature change <br /> #3 Bottom 78 . 7566 78 . 6658 x 25% + or . 0 i 5 Gallons <br /> Amountadd d or removed <br /> Avg . 80 . 2717 80 . 2321 to get Slope tube back <br /> to starting point . 018 <br /> Net loss or ain <br /> . 032 gallons <br /> Test #2 <br /> Thermometer Net Change Temperature shift <br /> Shift due to <br /> Start End + or - Temp. only Times Factor <br /> Time Temperature shift times <br /> 4k1 Top x 25% factor equals volume <br /> change due only to <br /> #2 Mid. x 50% Temperature change <br /> #3 Bottom x 25% + or - Gallons <br /> Amount added or removed <br /> Note: NEPA in Publication #329, 4-3.10.0 does not call for a to get slope tube back <br /> precision test to show a loss of more than .05 gallons to starting point <br /> (189ml) per hour. <br /> Therefore, since tested tank hada loss ain of (line 13) Net loss or gain <br /> . 032 gallons per hour it' DOES T meet NEPA gallons <br /> criterion for tightness. <br /> OIL EQUIPMENT SERVICE <br /> Division of Keith dustxial. , Inc. <br /> PO $0x. 950 - 750 Indus:t�iel. Way <br /> San Andreas ,".CA 95249 TESTER <br /> PHONE (209)754-1808 <br />