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27. <br />LOG OF LEST PROCEDURES <br />ISupplemental) <br />v LEADE <br />26• Record details of setting up 29. <br />DATE and running lest. luso fvN ,,, Reading <br />length of fine it needed.( ,. <br />TIME <br />Ile ht 1 <br />®�AVR �p n A.) J` ! 7"L� <br />30. HYDROSTATIC <br />PRESSURE <br />CONTROL <br />standpipe Level <br />In <br />M Mthes + <br />31. <br />VOLUME MEASUREMENTS M <br />RECORD 10 .001 GAt. <br />32. Product In 33. Product <br />Gradwle Replaced t-1 <br />34. <br />TEMPERATURE COMPENSATION <br />USE FACTOR la► <br />35. 36. 37. <br />Charnge Computation <br />Thermal Ihgher • IC) • la) + <br />Sensor lower - Espansion <br />Reading Id Cello action - <br />it iA c f - <br />-[—/--- <br />l/7 >3 �` 3ZI _ <br />38. NET votumE <br />CHANGING <br />EACH READING <br />famperature <br />Adwstmem <br />39. <br />ACCUMULATED <br />CIiAt E <br />' <br />At tow level Compute <br />Cha s r Hoa <br />(NFPA %ramal <br />volume Minus <br />[%pension I•) a <br />Conti 1) <br />p0(V1 — 1371T) <br />-- <br />�• lsI <br />BeginMng <br />of <br />Reade" <br />level to <br />'which <br />Restated <br />Beton Aller <br />Reading Reading <br />Product <br />Recovered 1'1 <br />1j' J eGI✓�J�:G.% INC.'I <br />i°..[✓dl <br />t <br />'! <br />''/L�/V <br />/�. <br />117-0 <br />nes <br />Z90 <br />7t )o <br />YS0 <br />2� <br />. Z90 - fJ0 <br />lit <br />/zg <br />17Z <br />MCI, <br />. CI, . K 70 <br />4 l90 _ <br />�3�� <br />z y7 <br />• osr/7� <br />.s <br />YS' z <br />//Z" <br />J Z.+ <br />.. g70 <br />f Za0 <br />/y8 <br />¢� <br />Z `i! <br />o OL___ <br />L <br />O /7 <br />35:5 <br />f: 4o <br />/ S % <br />9 <br />f Z Z Z <br />It 1,98 <br />f/98 <br />¢ 00'7 <br />o/7 <br />A 4 <br />,� ,� <br />P <br />�S� <br />-5 <br />.s/o 77S' <br />�: zoS <br />Z1s <br />// S <br />/73 <br />t8 <br />+8 <br />173 <br />.,J�3o <br />..�.L�c1..�.C' XL':s�L�i.�i <br />� <br />!S3 <br />' Z 30 .. y80 <br />I` ZSo <br />18 �_ <br />�'S <br />/9 <br />t <br />t. Z <br />05 <br />008 <br />-t:e>08 <br />ZGu.J ZZI /l!_ %�7- �U•l/eL)f <br />Z <br />!S® <br />/Z <br />- 7/y <br />t`Z30 <br />/70 <br />`� <br />ZZZ <br />I ZOo <br />ii sl <br />O <br />/z <br />�/ <br />f 2-30199 <br />_ <br />¢ ZL Z <br />¢ 008 <br />' ®a i <br />C>,/6 <br />foo'/ <br />/o yss' <br />t Z 5'S <br />Z -o ? <br />6?5- <br />Z o <br />z19- <br />1/0 <br />Z y 7 <br />2 <br />P -T Tank Test Data Chart . Tank <br />nk <br />Tank and product handling system has been tested light <br />Additional Info according to the Precision Test Criteria as established by <br />N.F.P.A. publication 329. This Is not intended to Indicate <br />permission of a leak. <br />O% <br />1. Net Volume Change at Conclusion of Preci on Test gph OR <br />® Tank and product handling system has failod the lank tightness <br />Signature of Tester: !rZ " /N� lest according to the Precision Test Criteria as established by <br />N.F.P.A. publication 329. <br />Dater L i e�•yE 88 <br />ONaat9 ' <br />v <br />11 is the responsibility of the owner and/or operator of this <br />system to Immediately advise state and local authorities of any <br />Implied hazard and the possibility of any reportable pollution 10 <br />The environment as a result of the Indicated failure of this <br />system. Heath Consultants Incorporated does not assume any <br />responsibility or liability for any loss of product to the <br />environment. <br />Tank Oyener/Operator <br />Date <br />J. <br />