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AINLAY'-,ANK TIGHTNESS TEST No. \J <br />10 INCLUDE ENOUGH INFO. TO ACCURATELY IDENTIFY TANK. (NUMBER/CONTENTS/POSITION, ETC.) <br />TANK I.D. � <br />TANK DIAMETER 9 <br />— 7 INS FILL PIPE LENGTH yir INS <br />WATER IN (a) START WATER IN TANK f� INS (c) END WATER IN TANK <br />TANK I (b) START WATER IN TANK 'e"' GALS (d) END WATER IN TANK <br />_INS <br />GALS <br />PRODUCT <br />TEST <br />(a) NOMINAL CAPACITY % Oo D 0 o GALS (c) DEDUCT WATER IN TANK _ GALS <br />o m <br />(b) ACTUAL CAPACITY i9V S L GALS (d =TAL PRODU T VOL. % A A31 GALS <br />VOLUME <br />(FROM TANK CHART) ov d it' <br />13 <br />(a) HEIGHT OF WATER TABLE ABOVE TANK BOTTOM = [✓ (h) INSFILL <br />(b) DENSITY OF TANK PRODUCT = (w) LB/CU. IN. (FROM TABLES) <br />DENSITY OF EXTERNAL WATER - 0.036 LB/CU. IN. <br />PIPE <br />(c) ADDITIONAL HEAD REQUIRED = (h) x 0.036 x 0.036 INSEXTENSION <br />--I_ <br />(w)NOTE: <br />IIIIIIIIII� ---I-- <br />I— <br />TO AVOID POSSIBLE TANK DAMAGE THE ADDED PRESSURE FROM A FILL PIPE EXTENSION MUST NEVER <br />EXCEED 5 P.S.I. AT THE WATER LEVEL. <br />14PRELIM <br />(a) START TEMP CHECK 7 , sp 01PM (d) A.P.I. GRAVITY 3 3, s AT �°F <br />(b) END TEMP CHECK 9_bd ®/PM (e) A.P.I. GRAVITY X16 5" AT 60°F <br />TEST DATA <br />(c) TIME SINCE LAST LIQ. ADDED � HRS (f) COEFF.OF EXPANSION -ObA yb'3/(m <br />15(a)STARTTEST <br />4f�D0 IPM:ENDTEST •O .IPM:TESTTIME�tL MINS. <br />DATA <br />(b) TOTAL TEMP. CHANGE (AVG END TEMP. — AVG START TEMP.) = 4 [u7 — 1�— + A ^F. <br />(c) VOL. CHANGE DUE TO TEMP = PRODUCT VOL x TEMP. CHANGE x COEFF. EXP. <br />(12dx ' d5bl x 0 QAA yn )4 It4n =+10-190 GALS. <br />(d) TOTAL LIQUID VOL ADDE SUBTRACTED AT END OF TEST ......................... GALS. <br />(e) VOL. CHANGE NOT DUE TO TEMP I(c) + (d)] ............ = ^r 1190 + 4410 =&/- _ 010 GALS. <br />(f) LEAK RATE = (e) x w _+4aG.P.H. <br />_ <br />TIME OF TEST (MINS) O LG (15a)j <br />THIS LEAK RATE DOES/DOES NOT EXCEED THE STANDARD OF 0.050 G.P.H. DESCRIBED IN NATIONAL <br />FIRE PROTECTION ASSOC., BULLETIN N.F.P.A. 329. <br />THE TANK IS TIGHT M / THE TANK IS NOT TIGHT ❑ <br />--I_ <br />IIIIIIIIII� ---I-- <br />(b) TOTAL TEMP. CHANGE (AVG END TEMP. — AVG START TEMP.) = 4 [u7 — 1�— + A ^F. <br />(c) VOL. CHANGE DUE TO TEMP = PRODUCT VOL x TEMP. CHANGE x COEFF. EXP. <br />(12dx ' d5bl x 0 QAA yn )4 It4n =+10-190 GALS. <br />(d) TOTAL LIQUID VOL ADDE SUBTRACTED AT END OF TEST ......................... GALS. <br />(e) VOL. CHANGE NOT DUE TO TEMP I(c) + (d)] ............ = ^r 1190 + 4410 =&/- _ 010 GALS. <br />(f) LEAK RATE = (e) x w _+4aG.P.H. <br />_ <br />TIME OF TEST (MINS) O LG (15a)j <br />THIS LEAK RATE DOES/DOES NOT EXCEED THE STANDARD OF 0.050 G.P.H. DESCRIBED IN NATIONAL <br />FIRE PROTECTION ASSOC., BULLETIN N.F.P.A. 329. <br />THE TANK IS TIGHT M / THE TANK IS NOT TIGHT ❑ <br />