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- THORNE ENVIRON TEL`1d0 .916-784-7496 Mayftw8 ,89 17 : 14 No .005 P -20 <br /> AIV 11Y TANK TIGHTNESS 1 ES'l 2, <br /> 18 INCLUDE ENOUGH INFO. TO ACCURATELY IDENTIFY TANK (NUMSFHICONTENIS,POSITION. ETC I <br /> TANK I.D. <br /> TANK DIAMETER ,W__9 15L /* _ INS FILL PIPE LENGTH _22-4--_-_,.. ...— INS <br /> 17 INS (Cl END WATER IN TANK __ _ .—___ IN5 <br /> WATERIN is)STARTWATER,NTANK _ -- <br /> (bl START WATER IN LANK _. �_ _-_GALS (di END WATER IN TANK ._ 1_ --__.._GALS <br /> 19 (a) NOMINAL CAPACITY .�Gl _- GALS IU DEDUCT WAFER IN TANK _._.._ GAL- <br /> I PRODUCT !n� ' <br /> I Ib)ACTUAL CAPACITY lr•e�wL,.••,^—GALS Im TOTAL PRODUCT VOL _,-I,._% .:__..- GALS <br /> VOLUME (FROM TANK CMARTI <br /> 19t-i <br /> (v) HEIGHT OF LSATER TABLE PROVE LANK BOTTOM r. -,`11J _ tb; INS <br /> (b)DENSITY OF LANK PRODUCT .-.. (h, LB,CU. IN FRQfA TABLk'5 <br /> FILL DENSITY OF EXTERNAL WATER _, -_ O.OSTi - LO CU IN <br /> PIPE ICI ADDITIONAL BEAD REOUIREOlu • U U?' U Ii:IG_ _. _ .. .. IL': <br /> M <br /> EXTENSION ,. <br /> I NOTE. <br /> TO AVOID PO.'•SIULF ?4NN DA MAI:F TIIG 6"I)FI) PHFSSIIAF Lrt:Ill A I '! 1 ,':LF Ff1LN'iIJ'JN M4 ',I NF. <br /> EXCEED 51",I ,:1111[ WAIEI'. L!.VfL ---- <br /> 20 C 1�' F'M dIAP; Ur.n,nL / AT <br /> PRELIM (a) START TEMF G: I:CK _ ......fEH �k<��; ...-.. <br /> -•'``1 Ibl ENE TEMPCHFCK ` l �/A'rN I..; AP: GP;.,,:-1 ./._�. AI LC'r I <br /> TEST DATA ,C, TIME SINCE I A". 00 ADDEO _,11-f _. HH" 0. C-00 t' Cf •kArJS.OIJ_'LLL•Li1 /. k_ <br /> 2, a 21 ,o) START TE&f IC~':ril... CIM 'Ni fND TI 1 I�. .1.L: 6-wo <br /> s 0 TEST TIME i --tAF I TEMP lw; 'i:':i Lill,I. 'EIA T- 'i NF •i.MT '+ <br /> y. , + AVG _ .._ r_-• <br /> DATA - <br /> r - <br /> , <br /> (bl TOTAL TEMP CHANGE(AVG END TEMP. -AVG START TEMP.) x���,� - L�JsL = * 1)37 •F. <br /> (C) VOL. CHANGE DUE TO TEMP = PRODUCT VOL /x 'TEMP. CHANGE vx COEFFF�. EXP C, <br /> x =1,nI x ,i.i1Di1�7 JL 1 ._:ril, a f��y{;JGALS <br /> FYI O (d1 TOTALLIQUIDVOL ADDEWSUSIRACTEDATENDOFTE51 . . . . . . . . �:L�.=.�_1_L.G6:S <br /> p O I c N•I J 1 _. ' ..- GALS <br /> a (e) VOL CHANGE NOT DUE TO TEMP IIF., , IU), -_..`....L ..�� 1.��1- • <br /> �j -- <br /> -. . .•� (1) LEAK RATE - -m W W = -., KE, G.P H <br /> TIME OF TEST (MINS' UL '•��' <br /> THIS LEAK RATE B:AeS/�Q]11_0JEXCEED THE STANDARD OF 0050 G P H hfiSCRIBEU IN IJATIONAL <br /> Ci FIRE PROTECTION ASSOC., BULLETIN N.F,P.A 32V <br /> THE TANK IS TIGHT Spy"IfTHE TANK IS NOT TIGHT <br />