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PAGE OF <br />DATE <br />r <br />LOCATION <br />ADDRESS ® 3 Co a NtA�y GLkS 11t oi. <br />r <br />CITY {— S I O C. l L �a _ <br />PHONE l V,3 - 0) u I <br />Horner <br />1 detector <br />WORK SHEET <br />CHART CALIBRATION <br />.05 0--- .025 ❑ <br />.05 0--' .025 ❑ <br />BEGINNING <br />ENDING <br />'27 7S <br />2 7/ <br />Test Stand 3 �-- <br />x <br />.3S 3l <br />30 30 3 0 <br />Temp. indicator: A B C r,29 33 <br />f <br />PE OF SYSTEM Vapor Recovery TYPE of COVER <br />one ❑ Suction � Manifold Y 0 N 0-- NONE III-` Concrete <br />Hand ❑ Turbine ❑ Siphon Y ❑ N � Stage 1 ❑ Stage 2 ❑ Blacktop B� <br />• _ Earth ❑ <br />CHART CAL •0S - �0 ` s 00 1-7.—(A) GRAPH COLOR <br />KNOWN AMOUNT AVERAGE j <br />OF PRODUCT CHART DISPLACEMENT ❑RED 9 SLUE <br />Vent Size c( <br />Fill Size 3 VL"— <br />Remote <br />Z `' <br />Remote Fill Y O N �0'� <br />Product Temp. <br />Measured Gravity .2 7. 3 <br />Coefficient Average 2s"ce <br />'B FACTOR <br />30oo x 00c) /s30 =/_ZS cel <br />TANK SIZE COEFFICIENT <br />LEVEL <br />START <br />LEVEL <br />END <br />TANK NO. <br />x (A) <br />FACTOR <br />PRODUCT CR <br />L �- <br />O` 5® l Y C� W (5"- <br />- I IOGHT OF: <br />I <br />Test Stand 3 �-- <br />x <br />Fill Pipe <br />3 <br />FINAL <br />RESULT <br />Y0 3t <br />TOTAL <br />TANK DIAM. - <br />WATER TABLE: 1 ql <br />WATER IN TANK Y <br />CI N �dnches <br />Vent Size c( <br />Fill Size 3 VL"— <br />Remote <br />Z `' <br />Remote Fill Y O N �0'� <br />Product Temp. <br />Measured Gravity .2 7. 3 <br />Coefficient Average 2s"ce <br />'B FACTOR <br />30oo x 00c) /s30 =/_ZS cel <br />TANK SIZE COEFFICIENT <br />LEVEL <br />START <br />LEVEL <br />END <br />GAIN* <br />LOSS- <br />x (A) <br />FACTOR <br />LEVEL <br />RESULT <br />TEMP <br />START <br />TEMP <br />END <br />GAIN♦ <br />LOSS- <br />_ �. <br />x <br />x 181 <br />FACTOR <br />. 2y <br />TEMP <br />RESULT <br />` S <br />FINAL <br />RESULT <br />Y0 3t <br />TIME <br />-7"00 L5' <br />='fre3G0IF <br />q <br />x .. <br />-:por <br />�4�5 <br />-25�� <br />_ �.�o/ <br />x <br />1.-�p�'� <br />'=c3cao� <br />VF <br />71 <br />21 <br />A <br />x .. <br />_ <br />x <br />�. <br />=-000(4 <br />- <br />7 <br />_ <br />_ ® <br />x .. <br />_ ® <br />2 Vu <br />_ - <br />= 4 0 Qy <br />x <br />-;� O l 3 <br />y- 0 o 1-3 <br />_Lka_2__ <br />'77 <br />x <br />-' C� <br />_.� L <br />_ `? <br />d <br />x <br />= o <br />-235' <br />= <br />x <br />= ® <br />= 0 <br />1 L .._ <br />�L <br />- 7L <br />= 0 <br />x <br />= v <br />S <br />- 23% <br />= <br />x <br />= v <br />_ <br />16Vr <br />• REMARKS: <br />- <br />Rate of loss al/hr. CERTIFY. Y �N ❑ <br />Operator(/-��-- C <br />