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Stability n2q Q$ <br /> R__��: PO� f P�I_�1L_ 6IVis TEST <br /> ���-_ T I <br /> D a t e-L12--10---/----- <br /> Company'__Csl�t/9sQ�c51�_�t�ltf __ Add resel�LasrQ-�L2�1�_GSS�4>�L------ <br /> Eir orripTirade of <br /> Name------------------------------------ Product__,�.ic St�f!---------------- <br /> 6-0 (Minute Temptratury Clleck ',// t�r� <br /> Starting -lime for Temperature CheckTMaM-tCompI * tion TimegtZ`_-4 <br /> --------- ----------�- -----------E----------F------ <br /> -------------- ____________.----_—_—___-------___—_-----_--- <br /> i__________________ ___---____ _ __---_--_---_—____---__- <br /> tika.rt End :Teo, Shiflr Flu IIiply : Add uFF• for <br /> of o'f ( {:' rroR, G7 : Column a Welglsted <br /> F'rot•e = Te=- t Test + or - 0b- , E Shaft <br /> r a2 t i ---- : 75 <br /> P 6. 0 ✓ ------------- <br /> -- -------------------- -------- <br /> Iliddle a Jro, oZ�_ ` S6 oZ �_ _,u -®- <br /> Y. <br /> PIC,ti-0-111 <br /> ----- �r-6=a7--- - S6' -- �" ins/ -------- --��--------- -- ----- <br /> ------------ <br /> Lire <br /> 1 . add the Three liesults rn Colunm F (lJeighled Hoe . Temp . 5hi { t ! . . . . . • • ._�_Q�_-___-. <br /> iy Q 'Temperature <br /> 2. Tank Ura . u Lyt ._____9:L_____ : ballon Capacity• • • • • • • • • _-�/ -- <br /> 3• Exact Mater Level in TankSLarl.-1 <br /> Bottom at Start of Test . . . . . . . . . . . . . at End =_- <br /> do Minute VOlUmt-ChtcK h;ud x-70 <br /> Start time_ C,Off, E• tion Time_g.5/60-14'�1 <br /> 4 . Exact Amount of Liquid Lost L fie ed (-! or Gained r. F <br /> O/ld Level. of. 'fest <br /> Removed (e ! in fill pipe to restore original level . . • . . ._______—_ - <br /> �I 5. HPI Gravity of 'rested Liquid in Graduate . . . . . . . . . . . . : . . . -- <br /> 6. Temperature of Tested Liquid in Graduate . . . . . . . . . . . . . . . . S _-- <br /> f <br /> 7. Subtract Line 6 from 600. (resull is a or -) . . .. . . . . . . . . . .____- _—_ Probe Settings <br /> 8. Multiply Line 7 x . 1 . _ , •7 <br /> q „ <br /> 9. Line 5 + or - Line 8 (APl Gravity " ' --�, -7 - Cyl7S/1 <br /> Adjusted for lemperature) . . . . . . . . . . • . . . . . . . . . . . . . . . . . . • _ _ _ <br /> 1n . With Line 9 enter Table C, " <br /> Read Coefficient of Expansion . . . . . . . . . . . . . . . . . . . . . . . . . . l -�_- <br /> 11 • Multiply Line 10 by Line 2 ((Talions) , <br /> Volume Change for Each Uegree of lemperature Change ) . .=__-� _ <br /> 12. Multiply Line 11 b>• Line 1 =fb S3 - <br /> (Volume Chanqe Due to lemperature) . . . . . . . . . . . . . . . . . . . . . _--- --- <br /> 13. Chanqstun of cine 12 (=-ee Sec . 9.4 . ) and add to Line 4 _ <br /> meUoubmetcheckYsigua Mlinu- ifnpr9oductslost ,aNOS if gained! <br /> NOTE: NFPA in Publication 0329, 4-3. 10 . 1 does not call for a precision test <br /> to show a < of more than .05 gallons ti89m1 ) per hour . <br /> Therefor e,, ted tants had a loss/ate of ( line 13) =��Yl- gallons <br /> per hour RW <br /> „� meet the NFPA criterion for lank tightness . <br /> Add i It ion aLdn' F�Ce <br /> kenr.rke w <br /> ----- <br /> Kk <br /> IV <br /> --------- '° M b� =y --------------------------------------------------- <br /> ------ T��Fq� �4 ---------------------------------------------- <br /> TV <br /> ------------- <br /> tT ------- <br /> ------------------------- <br /> �l Acruricy of lest is dependent on operator following instructions End results are the sole respoa i ity of the operator, <br /> WWAY lank 'legrity Tesler' is a registered Truk Neck of STI Services,lnc. Northbrook, IL 60062 <br /> AINLAY Tank 'Tegnty Taster <br />