COMPLIANCE INFO - Laserfiche WebLink

Home Browse Search

TANK ID to INCLUUE ENOUGH INFO. TO ACCURATELY IDENTIFY TANK. (NUM BER I CONTE NTSI POSITION, ETC.) TANK I.D. p PRODUCT I r Ci TANK DIAMETER ! L INS FILL PIPE LENGTH INS 11 WATER IN (a) START WATER IN TANK x INS (c) END WATER IN TANK INS TANK (b) START WATER IN TANK GALS (d) END WATER IN TANK rll� GALS 12 lal NOMINAL CAPACITY /%/J/1U GALS (c) DEDUCT WATER IN TANK � GALS PRODUCT (b) ACTUAL CAPACITY /5w GALS (d) TOTAL PRODUCT VOL. /OO.So GALS VOLUME (FROM TANK CHART) 13 (a) HEIGHT OF WATER TABLE ABOVE TANK BOTTOM = IN INS (b) DENSITY OF TANK PRODUCT = (w) LBICU. IN. (FROM TABLES) FILL DENSITY OF EXTERNAL WATER = 0.036 LBICU. IN. PIPE (c) ADDITIONAL HEAD REQUIRED itJR = (h) x 0.036 = x 0.036 = INS EXTENSION (w) NOTE: TO AVOID POSSIBLE TANK DAMAGE THE ADDED PRESSURE FROM A FILL PIPE EXTENSION MUST NEVER EXCEED 5 P.S.I. AT THE WATER LEVEL. 14 (a) START TEMP CHECK '%30 AMI139 (d) A.P.I. GRAVITY 32- S AT 57.0 'F PRELIM (b) END TEMP CHECK $15 AMIPM (e) A.P.I. GRAVITY 33•Y AT 60'F TEST DATA (c) TIME SINCE LAST LIO. ADDED /G f' HRS (f) COEFF. OF EXPANSION racac/SGvi 15 (a) START TEST AM/10: END TEST 4545 AM/FW. TEST TIME 941 MINS. TEST _ t� (b) SLOPE - (END TEMP — START TEMP) - mr \ — A=Zlr_vOS DATA TIME 9 (c) TEMPERATURE CHANGE DURING TEST = (SLOPE OF "BEST FIT' LINE) x (TEST TIME) = ao0511L% x 90 - =+/r .OVG 'F. (d) VOL. CHANGE DUE TO TEMP = PRODUCT VOL x TEMP. CHANGE x COEFF. EXP. _ = 10050 tlzex '—OY6' 05DI x,pae YSGyl Ukl- ID GALS. (e) TOTAL LIQUID VOL. ADDED/iMS111111hOf6111, AT END OF TEST ....................... _ ' I' • 17.3 GALS. (f) VOL. CHANGE NOT DUE TO TEMP I(c) + (d))...... _ -210 4-037- GALS. (9) LEAK RATE = lel x eo = .037 x eo = 7'-0-2-Y G.P.H. TIME OF TEST (MINS) 96 psel - THIS LEAK RATEAW/DOES NOT EXCEED THE STANDARD OF 0.050 G.P.H. DESCRIBED IN NATIONAL FIRE PROTECTION ASSOC. BULLETIN N.F.P.A. 329. THE TANK IS TIGHT 0 / THE TANK IS NOT TIGHT ❑ 16 NOTES JAN t :/