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AINLAY 1, AK HIGH"FNESS FEST Nc ------
<br /> -AIN, �YTANK TIGHTNESS -rEST o.
<br /> ...............
<br /> 10 INCLUE)E ENOUGH INFO. TO At IDENTIFY rANK. (NUMBERiCONFENTS/POSITION, Ercj
<br /> TANK I.D. lANKDIAMEIE_'R 16 INCLUDE ENOUGH INFO. TO ACCURATELY IDENTIFY TANK, (NUMBER/CONTEN TS!POSIT ION, ETC.)
<br /> ....... INC, FILL PIPE LENGTH TANK I.D. TANK DIAMETER
<br /> _f INS ................ FILL. PIPE LENGTH ------------ INS
<br /> WATER IN (a)START WATER IN TANK INS (c)END WATER IN TANK 17
<br /> LANK (b)STAHT'WAl ER IN TANK,_._... I N S -TER IN a)START IN TANK
<br /> G A L S (d)ENDWATER IN TANK GALS WA INS (c)END WATER IN TANK INS
<br /> TANK (b)START WATER IN TANK GALS (d)ENDWATERiN TANK GALS
<br /> >
<br /> �a) NOMINAL CAPACITY
<br /> ._..Z 0
<br /> PRODUCT W-1..... GAILS �c,) L)EDUCTWAT ERIN TANK
<br /> G 4 L
<br /> (t))AC,T UAL CAPACI TY iAlLS �d) TOTAL PRODUCT VnL. PRODUCT (a) NOMINAL CAPACITY (c)DEDU(.,J WA TER IN TANK
<br /> VOLUME GALSin
<br /> (FROM TANK CHART) (b)ACTUAL CAPACI rY G A!.S (d) TO!At.. PRODUCT VOL GALS
<br /> VOLUME
<br /> (FROM TANK CHAR I) GALS
<br /> 19
<br /> (a) HEIGHT OF WATER TABLE ABOVE TANK BOT I'ONI
<br /> _. )ii (n0 INS
<br /> FILL (I.)) DENSI TY OF TANK PROD U C r W IN (FROM rAI]ILES) (a! HEIGHT OF WATER TABLE ABOVE TANK b(JT7(,M (I)) INS
<br /> 0036 (I)) DENSITY OF TANK PRODUCT
<br /> DENSITY OF EXTERNAL WATER L B C U. I N. FILL (vv) LB;CU IN (FROM TABLES)
<br /> PIPE: (c) ADDITj(,)I,4At,. HEAD REQUIRED DENSITY OF EXTERNAL VVAI ER 0 10 6
<br /> (h) x 0 036 0�0 3 6 1 N S 3 L B i C U IN.
<br /> c) ADDrrioNAL. HEAD RE,'QUIFIE0 x 0.036
<br /> EXTENSION PIPE Ih� x 0.036
<br /> .................. --------
<br /> NO 1 E: INS
<br /> EXTENSION (N)
<br /> I() AVOID POSSIBLE TANK DAMAGiE THE ADDED PRESSURE FROM A FILL PIPE EXTENSiON MIjSf NFVEIdNOTE:
<br /> EXCFED 5 PS.1 AT THE' WATER LEVEL,
<br /> TO AVOID POSSIBLE TANK DAMAGE THF At E)FID PRESSURE From A FILL PIPE EXTENSION MUST NEVER
<br /> EXCEFD ,) P,S,i, AT THE WATER LEVEL
<br /> ( RT I EMP40�pm Id) A,P.I GRAVITY 20
<br /> PRELIM p
<br /> T E 1,0 P i E K 2, (a) START TEMP CHECK
<br /> C.2 A N1 �e) A.P.I.AGRAVITY t AM,PM (d) A.P.I. GRAVITY AT
<br /> 1 E., t'' DA, A
<br /> If PRELIM
<br /> 'i'1ME E: I N T L A D E 1) ib) END TEMP CHECK Am;Fly,
<br /> (e� A,P.! G R AV I TY
<br /> 'FEST DATA (c) T ME SINCE LAST iJO ADDED
<br /> HHS I.:,FF 0 F E X P A N S 1100
<br /> ....... COEFF,OF EXPANSION
<br /> 5
<br /> END rf,"S'T
<br /> A M 2 1
<br /> r Ti�,/,F
<br /> I AR TE�.�;
<br /> A M- E NIL) TES!' AMPM `FST TIME
<br /> ..............
<br /> T E Y p i
<br /> �,M F ,j E77 j 1_, I TEST
<br /> 0
<br /> I _T_
<br /> G TE -t-y.p I-tv' E m p vVTD�
<br /> 1 7 F , -%I,- I
<br /> A mp t
<br /> AT T� A
<br /> 3 AVG,
<br /> . ......... .........
<br /> ----------
<br /> . .. .. ........
<br /> +
<br /> J.)_
<br /> ------------
<br /> >
<br /> 4-
<br /> z ---------
<br /> 2
<br /> 2
<br /> ... ..
<br /> a ........c_ ,82— <
<br /> ---------- ------------
<br /> ...........
<br /> ............ .......---
<br /> ..........
<br /> ............. .......... ...............
<br /> ...........
<br /> (b) TOTAL TEMP,CHANGE(AVG END-TEMP, AVG START TEMP.) °F.
<br /> (b) TOTAL TEMP.CHANGE(AVG END TEMP, —AVG START TEMP.) -F.
<br /> (c,) VOL (,HAN(-',E DUE TO TEMP PR-ODUCT VOI_ x TEMP. CHANG l E x (OEFF. EXP (c) VOL. CHANGE DUE TO TEMP PRODUCT VOL x TEMP. CHANGE x COEFF. EXP.
<br /> x JX�1x i5u_ � -
<br /> (:aALS,
<br /> �21
<br /> (d) TOTAL,LIOUIDVOL,ADDED/suBrPACTEDAT ENE)OF TEST . . . . . uj GALS.
<br /> . . . . . . GALS.S. cr (d) TOTAL,LIQUID VOL,ADDED/SUBT RACTED AT END OF TEST
<br /> cx) a
<br /> C) 0 .. . . . . . GALS.
<br /> (e) V01
<br /> CHANCE NOT-DUE TOTEMP (cl)], I GALS. < (e) VOL.CHANGE NOT DUE TO TEMP f(c) +
<br /> j.111, -- --
<br /> G,P.H. (e) x 60 x 60LAK RATE (e) x w . . . . .
<br /> (f) LEAK RATE
<br /> G.P.H.
<br /> e, LEAK RATE DOESIDOES NOT EXCEED THE STANDARD OF 0,050 G P,H �71
<br /> THIS LE f")ESCRIBED IN NA f IONAI.
<br /> TIME OF TEST (MINS)
<br /> FIRE PROTECTION ASSOC,, BULLEfIN N.F,P.A, 329, THIS LEAK RATE DOESIDOES NOT EXCEED THE STANDARD OF 0.050 G.P.H. DESCRIBED IN NATIONAL
<br /> THE TANK IS Tj(�H_r THE TANK IS NOT' TIGH T 1 FIRE PROTECTION ASSOC., BULLETIN N,F,P.11 P.A. 329.
<br /> THE TANK IS TIGHT' THE TANK IS NOT TIGHT
<br />
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