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rner Ho <br />PAGE oZ OF �_ ECHE- <br />DATE. O 9' 3' i it� detector <br />WORK <br />WORK SHEET <br />LOCATION <br />ADDRESS - - <br />v ) <br />CITY <br />L -J <br />A, c 'J <br />PHONE <br />Temp. Indicator: A B C D <br />CHART CALIBRATION <br />.05 ❑ .025 ❑ .050 .025 ❑ <br />BEGINNING ENDING <br />TYPE OF SYSTEM - Vapor Recovery TYPE of COVER 1 <br />one ❑ Suction O Manifold Y ❑ N ❑ NONE ❑ Concrete ❑ <br />I* <br />Hand ❑ Turbine ❑ Siphon Y ❑ N ❑ Stage 1 ❑ Stage 2 ❑ Blacktop ❑ <br />Earth o 'B FACTOR <br />CHART CAL ' - (A) GRAPH COLOR <br />KNOWN AMOUNT AVERAGE i X (B) <br />QF PRODUCT CHART DISPLACEMENT❑RED ❑BLUE <br />I TANK SIZE COEFFICIENT <br />r <br />Vent Size <br />Fill Size <br />Remote Fill Y ❑ N ❑ <br />Product Temp. <br />Measured Gravity _ <br />Coefficient Average _ <br />LEVEL LEVEL GAIN• <br />START END LOSS- <br />x (Al <br />FACTOR <br />TANK NO. <br />TEMP TEMP GAIN♦ <br />START END LOSS- <br />PRODUCT <br />o( C <br />HEIGHT OF: <br />Test Stand <br />Fill' Pipe <br />TOTAL <br />TANK DIAM. <br />WATER TABLE: <br />l <br />WATER IN TANK Y U N ❑ Inches <br />Vent Size <br />Fill Size <br />Remote Fill Y ❑ N ❑ <br />Product Temp. <br />Measured Gravity _ <br />Coefficient Average _ <br />LEVEL LEVEL GAIN• <br />START END LOSS- <br />x (Al <br />FACTOR <br />LEVEL <br />RESULT <br />TEMP TEMP GAIN♦ <br />START END LOSS- <br />x IBI <br />FACTOR <br />TEMP <br />RESULT <br />FINAL <br />RESULT <br />TIME <br />=t-ooc, <br />l <br />f:0O'3 x <br />'l; vo 3S <br />=f-ocjo <br />/Loo _ <br />C. I = f L x <br />*�v la 3 L <br />=f• -o o o fo <br />--0016 <br />- = t Jo f x <br />ol3 <br />=70003 <br />It(o! L <br />L -gyp = -� x <br />.. <br />r dol 6 <br />- _ �,o,� L x <br />yrOa t <br />y: oo ( <br />tel <br />(3 <br />% x <br />•• <br />7, oulfr <br />x <br />- i(i0 <br />•• <br />_`l`rJ lu3 <br />f <br />=-7 -0003 <br />L 11.4 <br />— = x <br />- <br />— x <br />.. <br />_ <br />— = x <br />.. <br />- <br />— = x <br />_ <br />_ = x <br />_ = x <br />.. <br />_ <br />_ = x <br />= <br />_ <br />— = x <br />•• <br />_ <br />— - x <br />= <br />— = x <br />.. <br />_ <br />— - x <br />= <br />_ <br />— = x <br />= <br />— = x <br />= <br />_ <br />— = x <br />= <br />— x <br />_ <br />REMARKS: Rate of loss gal/hr. CERTIFY. Y Er N ❑ <br />Operator <br />V <br />