Laserfiche WebLink
27. <br /> Sensor Calibration i 30. HYOROSTATIc31 34. 38.NET VOLUME 139. <br /> PRESSURE VOLUME MEASUREMENTS IV) TEMPERATURE COMPENSATION CHANGING ACCUMULATED <br /> LOG OF IESr PROCEDURES CON IIIOL RECORD TO,ODI CAL. USE FACIOR Tal EACII READING CHANGE <br /> 28. Record details of sellingu 29. Slandpipe Level Product in Pr Temperature <br /> p 32. 33. oducl. 35. 36. 37. <br /> DATE' and runninglest.(Use lull Reading in Inches Graduate Replaced I-) Adjustment <br /> length of Thermal line ft needed.) No. Beginning Level to Change Computation- <br /> Iligher• (c).(al• Volume Minus At Low Level comput <br /> TIME of which Before Alter Product Sensor Lower- Expansion• Expansion p'or Change 124 hr.I PRODUCT A' Reading Id Contraction- Contraction ) e per Hour <br /> S Up(l�-wtc Reading Restored Reading Reading Recovered I�1 s33(V)�—a37(TI (NEPA erilerlal <br /> °O ARRIVED AT:SITE REMOVED OP- rUBE,'VAPOR RECOYE RY LINES,BLEED REMOTE. PPS ETC <br /> q°0 SET-UP EQUIPMENT <br /> qi5 START CIRCULATION FACTOR "A"' (All C 41- <br /> 1ST THERMO READING 421 <br /> START 42° HIGH LEVEL TES ,top ( ,tp j <br /> 10n 1ST HIGH LEVEL READING 1 42 .1 IVO -- COO b51 + IS t Z3 <br /> 1b3® CONT'D HIGH LEVEL READING 2 42 <br /> 3 42 <br /> .0')o +14 t-05� _ q <br /> ' tom re rr 4 <br /> 42 Yj 0 -OQ25 42 <br /> ' 032. <br /> 1 ° er rr 6 42 . (to -A X0-7 <br /> g7 42 t75 t�l� -11(9 <br /> gob '° e. <br /> 8 42 12 - 0(0 • "12 <br /> oo DROP TO LOW LEVEL,WAIT 1 HO R <br /> START LOW LEVEL TEST <br /> 1 1ST'—LOW'—,—LEVEL—'READING 1 12 12' <br /> . 020 iso 102-1 <br /> 1240 CONT°D LOW LEVEL READING 2 12 <br /> 1Z� of re 3 t 5 �' o/ -oo7 - :003 <br /> 12 . 1 + ®0 1ST Q ( - <br /> 00a- - <br /> 4 12 . 1 2� 11oZ k4- �D <br /> er °° 5 12 . 1�� + 1' 1 J +/o/3 +,004- -1-000 <br /> Oa 6 12 . . t oI5 10 +4 x D(7 I -tam <br /> er rr <br /> 12 .Zig f. 15 '773 k4 + 17 -ooZ- —004 <br /> 12 . 231; a.CQO 773 1:0( <br /> 9 12 <br /> .no <br /> 10 12 .q-� 4-Q(a 1`83 a-3 +,�/3 J <br /> ll <br /> 12 . 275 4--0)0 IS kZ amu <br /> °t 12 12 ,�` OC�7 .7 k 3 )3 -p(� 7- <br /> 13 12 iZ�S 1,0110 7q0 +2 60S ooZ too4 <br /> n . <br /> 14 12 . 305 +,Q10 Q10 712- 47, ;ooF -too-,- <br /> 1 , <br /> 1 12 ,32o t_o(5 -795 k5 4.v zona- - <br /> " If 16 —12 .33D 4oto -07 1.2 tvo B i oo <br /> 17 12 _� sols 800 <br /> it - 18 12 43 <br /> �o 15 �U3 +3a3 �Z -�14- <br /> n <br /> 19_ 12 .. , 370 .--.Q10 . -fJ -f0/3 C>03 +0!i <br /> r. r. <br /> 20 128()q t.0/ +3 -to 13 <br /> 21 12 X3,10 67o 80 +Z- <br /> 22 <br /> Z22 12 4vo �-.0/0 <br /> rr <br /> 1° 213 12 .4-1 Z) �-.0 10 <br /> 24 12 4.0/0 X17 <br /> STOP TEST <br /> 6 --2=(]. )G PH <br /> ANIL <br /> Statement:2. � <br /> P-T Tank Test Data Chart It Is the responsibility of the owner and/or operator of this <br /> Additional Into Tank and product handling system has been tested light system to Immediately advise state and local authorities of any <br /> according to the Precision Test Criteria as established by Implied ha;:ard and the possibllilyof any reportable pollution to <br /> regulatory agency.This is not Intended to Indicate permission the environment as a result of the indicated failure of this <br /> G of a leak. system.The manufacturer of this lest method does not assume <br /> OR any responsibility or liability for any loss of product to the <br /> 1. Net Volume Change at Co clualon Pr sl est gph environment. <br /> ❑ Tank and product handling system has failed the tank tightness <br /> Signature of Tester: lest according to the Precision Test Criteria as established by -n <br /> (� a regulatory agency. Tank Owner/Operator 1` <br /> Date: <br /> OR <br /> ❑ Test Invalid due to environmental or mechanical factors beyond Dale <br /> control Qa lire testing equipment, <br />