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AINLAY T <br />INFO. TO <br />TANK I.D. I <br />TANK DIAMETER <br />K TIGHTNESS TEST No. <br />qS <br />Y IDENTIFY TANK. (NUMB <br />INS FILL PIPE LENGTH <br />(POSITION, ETC.) <br />4/9 _ INS <br />1INS <br />1 <br />WATER IN (a) START WATER, NS (c) END WATER IN TANK WATER,IN TANK <br />TANK (b) START WATER IN TANK GALS (d) END WATER IN TANK n GALS <br />12 )NOMINAL CAPACITY %S; QD GALS (c) DEDUCT WATER IN TANK Q GALS <br />PRODUCT (a <br />VOLUME (b) ACTUAL CAPACITY �` �✓ GALS (d) TOTAL PRODUCT VOL. '%? �� GALS <br />(FROM TANK CHART) <br />(a) HEIGHT OF WATER TABLE ABOVE TANK BOTTOM = (h) INS <br />(b) DENSITY OF TANK PRODUCT = (w) LBICU. IN. (FROM TABLES) <br />DENSITY OF EXTERNAL WATER = 0.036 LBICU. IN. <br />(C) ADDITIONAL HEAD REQUIRED = (h) x 0.036 = x 0.036 = INS <br />(w) <br />NOTE: <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 />14 <br />(a) START TEMP CHECK •• IPM <br />PRELIM " <br />(b) END TEMPCHECK %.�� AM49M <br />TEST DATA I (c) TIME SINCE LAST LIQ. ADDED 1— HRS <br />TEST <br />DATA <br />(a) START TEST AM10.. END TEST <br />(d) A.P.I. GRAVITY AT (%L D 'F <br />(e) A.P.I. GRAVITY 6 AT 60-F <br />(f) COEFF. OF EXPANSION . CCO 169rd& <br />AMl +6'. TEST TIME 60 MINS. <br />(h) TOTAL TEMP. CHANGE (AVG END TEMP. —AVG START TEMP.) = •J_L -•40 _ • 40622 F. <br />(c) VOL. CHANGE DUE TO TEMP = PRODUCT VOL x TEMP. CHANGE x COEFF. EXP. <br />x . �•c+X+sol x . 00o GG6T6++<�� +I - . Q GALS. <br />(d) TOTAL LIQUID VOL. ADDED/SUBTRACTED AT END OF TEST .............. ..... _ +,Q .01' GALS. <br />(e) VOL. CHANGE NOT DUE TO TEMP I(c) + (d)] ............ = • O i? + _ 66S = +10.638 GALS. <br />(f) LEAK RATE _ (e) x 60 7'6 3 8' x 60 a 038 G.P.H. <br />TIME OF TEST (MINS) 6 o 1+5a) <br />THIS LEAK RATE DES NO EXCEED THE STANDARD OF 0.0.50 G.P.H. DESCRIBED IN NATIONAL <br />FIRE PROTECTION ASSOC-.-, BULLETIN N.F.P.A. 329. <br />THE TANK IS TIGHT LTJ'/ THE TANK IS NOT TIGHT L] <br />�D�J►I�FZ�1�,��33�iiiii <br />:irzm <br />-/j�J�CJI_---_--�_� <br />-����-III�I/-�y�JI�llli�J- <br />FA970 <br />1APAM <br />Illillllilllllilllilll- <br />iiiii <br />-il�Illlilllli <br />Illlillll_Illlil-i <br />(h) TOTAL TEMP. CHANGE (AVG END TEMP. —AVG START TEMP.) = •J_L -•40 _ • 40622 F. <br />(c) VOL. CHANGE DUE TO TEMP = PRODUCT VOL x TEMP. CHANGE x COEFF. EXP. <br />x . �•c+X+sol x . 00o GG6T6++<�� +I - . Q GALS. <br />(d) TOTAL LIQUID VOL. ADDED/SUBTRACTED AT END OF TEST .............. ..... _ +,Q .01' GALS. <br />(e) VOL. CHANGE NOT DUE TO TEMP I(c) + (d)] ............ = • O i? + _ 66S = +10.638 GALS. <br />(f) LEAK RATE _ (e) x 60 7'6 3 8' x 60 a 038 G.P.H. <br />TIME OF TEST (MINS) 6 o 1+5a) <br />THIS LEAK RATE DES NO EXCEED THE STANDARD OF 0.0.50 G.P.H. DESCRIBED IN NATIONAL <br />FIRE PROTECTION ASSOC-.-, BULLETIN N.F.P.A. 329. <br />THE TANK IS TIGHT LTJ'/ THE TANK IS NOT TIGHT L] <br />