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«. - •�. avuIrrmcm1 aarvn;t „1lIruy idlIK eg11Ly Ieswr <br /> + [IMsion of Keith A. TOW Inc. REPORT <br /> 750 Industrial Way . P. Cl. sox 95 <br /> SAN ANORFAS, CALIF. 95249 Date <br /> (209)754-1808 <br /> Company Sav-Mor Oil 11307 Address 4579 E . Acampo Rd . <br /> Brand Name Grade of Product Unleaded <br /> Gallons 8131 API Gravity 56. 36 Coefficient of Expansion . 00066 <br /> Coefficient of expansion x gallons = Factor to be used in this test for each <br /> degree of temperature shift <br /> Factor 5 . 36646 <br /> Test IIX 3 <br /> Thermometer Net Change Temperature shift . 05875 <br /> Shift due to <br /> Start End + or - Temp. only Times Factor = . 3152 <br /> Time 12:06 1 : 06 <br /> Temperature shift times <br /> 111 Top 86 . 135 86 . 265 + . 13 x 25% •0325 factor equals volume <br /> change due only to <br /> 112 Mid. 81 . 585 81 . 615 + .03 x 50% .015 Temperature change <br /> 113 Bottom 79 . 525 79 . 52 + .045 x 25% •01125 6�or _ 315Gallons <br /> Vapor Build up during test Amount added orremoved <br /> to get Slope tube <br /> to starting point . 13 <br /> Net 67sDor gain <br /> 185 gallons <br /> Test IN4 I <br /> Thermometer Net Change Temperature shift-0125 <br /> Shift due to <br /> Start End + or - Temp. only limes Factor = . 06708 <br /> Time 1 6:09 7:09 <br /> 111 Top 86 .675 86 . 695 + .02 x 25% Temperature shift times <br /> .005 factor equals volume <br /> change due to <br /> 112 Mid. 81 . 715 81 . 715 0 x 50% 0 Temperature change <br /> 113 Bottom 79 . 065 79 .095 + . 03 x 25% .0075 � r - .067 Gallons <br /> Amount added or removed <br /> Note: NEPA in Publication 1)329, 4-3.10.0 does not call for a to get slope tube ac <br /> precision test to show a loss of more than .05 gallons to starting point .056 <br /> (189ml) per hour. Net los or gain <br /> Therefore, since tested tank ha a los gain of (line 13) <br /> 011 gallons per hour it DES )NOT meet NFPA .011 gallons <br /> criterion for tank tightness. <br /> TesterAiv--o <br />