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27. <br />Sensor Calibration / <br />LOG OF TEST PROCEDURES <br />30. HYDROSTATIC <br />PRESSURE <br />CONTROL <br />31. <br />VOLUME MEASUREMENTS(V)TEMPERATURE <br />RECORD 10.001 GAL. <br />34. <br />COMPENSATION <br />USE FACTOR (a) <br />38. NET VOLUME <br />CHANGING <br />EACH READING <br />39. <br />ACCUMULATED <br />CHANGE <br />28. <br />DATE <br />(21 hTIMr.) <br />Record details of sellingu P <br />and running test (Use full <br />length of line it needed.) <br />28• <br />Reading <br />No. <br />Standpipe Level <br />in Inches <br />Beginning Leval a <br />of which <br />Reading Restored <br />32. Product in <br />Graduate <br />Delors After <br />Reading Reading <br />33. Produce <br />Replaced (-) <br />Product <br />Recovered 1+) <br />35. <br />Thermal <br />Sensor <br />ikatllnq <br />36. <br />Change <br />Higher+ <br />Lower - <br />Irk <br />37. <br />Computation <br />1c) • (a) = <br />Expansion • <br />Contraction - <br />Temperature <br />Adjustment <br />Volume Minus <br />• <br />Expansion (1 or <br />Contraction 1-1 <br />eAV) — WIT) <br />At Low Level compute <br />Change per Hour <br />(NF PA criteria) <br />y <br />/� <br />m <br />,� <br />r2 <br />,o <br />1 0 <br />),o/o <br />'2 ,3 <br />.� <br />-gzr <br />�i <br />o pe <br />ej <br />I Z <br />`2'� <br />/O Ll <br />D..10 <br />_ <br />_ <br />IG.'ZS <br />,,01? <br />H <br />y <br />-�41d <br />1.01,91 <br />)l?'f <br />t <br />1" -,I2.3 <br />2,((o <br />2 S`"6 <br />f ®/G <br />'� 12 <br />L �{ <br />_ d 1 'l <br />= 7 <br />, 1-3 v <br />'I <br />I <br />W..b <br />5'2 <br />.S'2a . <br />5'r <br />2 <br />u7gd <br />Ca 6 <br />_b/0 <br />ZS <br />- 0/5- <br />2 <br />1 <br />� 20 <br />-5 3 j <br />) 01a <br />.5 6 <br />1-1,4 <br />l ®y z. <br />�l <br />'12, <br />12 <br />-f-310 <br />S-5 d <br />t <br />696 0, <br />116 <br />UqZ <br />a tYZ <br />'7Z <br />�-7 jj <br />.�-11d <br />t)/0 <br />(07 d, <br />/rJ <br />0,V. Z- <br />."-d�Z <br />12,2 <br />1 z <br />0 <br />3/0 <br />t,GZo <br />'l2 <br />.02 <br />0-0.5" <br />A <br />� :l <br />yL <br />.. d <br />�+�v <br />j0 <br />� 0 <br />� <br />6-3 q <br />—, t�2 <br />7" Z <br />226 <br />3Y6 <br />/,67o I <br />F2z <br />4 -It <br />1_60 <br />J oc3 <br />r <br />Z 3 <br />12 L <br />3 q io <br />-3 y <br />l' <br />S-* <br />r <br />—, 06!5 <br />`-, 7/ <br />310S, <br />I f <br />A <br />/r <br />2 <br />J 6 �r <br />L'' <br />-� <br />1 2Z <br />61-V <br />0 <br />�., a� 1� <br />J% t tY <br />Y 1 ( <br />�• t/ i t7 <br />1 l � <br />l7 <br />3 G <br />2 V,d <br />) o <br />?2 <br />U <br />0/� <br />- � <br />y <br />020 <br />X10 <br />3 Ll <br />G <br />0 z <br />-� . 0 /S <br />-- <br />��o <br />0-0 <br />J0 <br />: 0 to <br />1.93 <br />C <br />}, d /7 <br />, UGC <br />P•T Tank Test Data Chart 2 Statement: It is the responsibility of the owner and/or operator of this <br />Additional Into <br />13 Tank and product handling system has been tested tight system to immediately advise stale and local authorities of any <br />according to the Precision Test Criteria as established by implied hazard and the possibility of any reportable pollution to <br />N.F.P.A. publication 329. This is not intended to indicate the environment as a result of the indicated failure of this <br />�_ permission of,a leak, <br />0 system. Heath Consultants Incorporated does not assume any <br />`. OR responsibility, or liability for any loss of product to the <br />1. Net Volume Change at Co lusj of Pre i n est _gph environment <br />Tank and product handling system has failed the tank tightness <br />Signature of Tester: �;ast according to the Precision Test Criteria as established by <br />N.F.P.A. publication 329. Tank Owner/Operator <br />nate:1_I_ -� <br />i <br />Fn`—S <br />l� <br />y <br />/� <br />m <br />,� <br />r2 <br />,o <br />1 0 <br />),o/o <br />'2 ,3 <br />.� <br />-gzr <br />--0// <br />o pe <br />I Z <br />`2'� <br />/O Ll <br />,,01? <br />H <br />-�41d <br />1.01,91 <br />)l?'f <br />t <br />1" -,I2.3 <br />2,((o <br />2 S`"6 <br />f ®/G <br />'� 12 <br />L �{ <br />_ d 1 'l <br />= 7 <br />, 1-3 v <br />7 <br />%2.% <br />2 <br />'7.S�O <br />Ca 6 <br />_b/0 <br />ZS <br />- 0/5- <br />12,2 <br />1 z <br />0 <br />3/0 <br />t,GZo <br />'l2 <br />.02 <br />0-0.5" <br />7" Z <br />226 <br />3Y6 <br />/,67o I <br />F2z <br />4 -It <br />1_60 <br />J oc3 <br />Z 3 <br />12 L <br />3 q io <br />-3 y <br />t 0 2c <br />S-* <br />/ Z Zs- <br />—, 06!5 <br />`-, 7/ <br />310S, <br />I f <br />A <br />/r <br />2 <br />12,1 <br />17- <br />3_ ti <br />%0 <br />,� 08 <br />1 �;3 Z <br />!{ <br />1,617 <br />"- ? <br />- '%9-� <br />P•T Tank Test Data Chart 2 Statement: It is the responsibility of the owner and/or operator of this <br />Additional Into <br />13 Tank and product handling system has been tested tight system to immediately advise stale and local authorities of any <br />according to the Precision Test Criteria as established by implied hazard and the possibility of any reportable pollution to <br />N.F.P.A. publication 329. This is not intended to indicate the environment as a result of the indicated failure of this <br />�_ permission of,a leak, <br />0 system. Heath Consultants Incorporated does not assume any <br />`. OR responsibility, or liability for any loss of product to the <br />1. Net Volume Change at Co lusj of Pre i n est _gph environment <br />Tank and product handling system has failed the tank tightness <br />Signature of Tester: �;ast according to the Precision Test Criteria as established by <br />N.F.P.A. publication 329. Tank Owner/Operator <br />nate:1_I_ -� <br />i <br />