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i=ll E 0 Z 0 -b te— 0 Z .1 r -=a v- t-- Ic:� i sx :i. c:) A L. k "T <br />Fes. ri. F9.5 x 0130 +: *i li—I.< ar-19 r i . Lir . e-1F� Sas ak;n c ao.,e. ) <br />Invoice No.: 1; 883A Date: 0,-a/123/91 Time : 08:03:E:7 <br />Technician: BWH Tank: 1 Tank Diameter(in): 95 <br />Volume(gal) : 10000 Grade Level (in) : 1,351 product Level (in): 133 <br />Water Level On Tank(in): 0 <br />Specific Gravity: CII. 75 Coefficient Of Expansion: 0. ('70066 ,8 <br />Calibration Value(ml): 378 Channel: 1 <br />Level Segment From: ]. To 225 Temp Segment From: 1. TO 12,0 <br />..................................... ........ ........... ............. il.................. u ...... ............................... ............ ,. r.. ,...,....... 4.a.a.......... ...... ..... .............. .�....�.........,................ <br />......,...............��...�.�..�.... <br />ft ,r I .. rtu t ., t ,...ut..,. .t�tl x.. ., iter•• i <br />I.I <br />i <br />t:'....a............................................ . ...... . � ........,..,.....,............... .,.... .,... ................ ...,...... ....,,............................ ..... ............ .._........�.a.... <br />„�,..I, I i i �;;:� ...,.Iii .I, I,,.i i..,l I, �;;:� .;::• <br />Change In Calibration Zone = 15 <br />Starting Temperature (F)-. 62.165 <br />Surface Area(sq. in): 151.4 <br />Level volume (gph) : V1.04 <br />Temp. volume (gph) : 0.09 <br />Net change (gph) : -0.05 <br />FR ee is. e -t 1 -b -- -- ? F=I 1=1 is S3 <br />Calibration Unit (gal/unit) = 0.00655 <br />Head pressure (eal/in (Dtm)) : 99.7 <br />Temp. Change (F/h) : 0.014 <br />Product Line (gph) : --.003 <br />•t4* Notes * <br />WEST LANE= FUELS 3300 WENT LANE: STOCKTON, C.A. <br />THIS IS A HIGH LEVEL_ `I TEST WITH A �R'X-C:AL. SND HR. <br />