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08/19/2014 07:39 20936754?4 BAGLEY ENTERPRISFS PAGE 04/04
<br />�fforda-Te_c
<br />416 2`1 Street
<br />Galt, Ca 95632
<br />,'hone: (209) 744-0112
<br />Fax: (209) 744-0116
<br />.-,r# .Y.■n_net
<br />TP 201,3B ort Form.
<br />AST Static Pressure PerformanOm'Test FFo�n TEST
<br />CO F# 12-14726 ZANE "111"0 , y
<br />N-913-1-] Technician:
<br />permitvumberON METRO AIRPORT
<br />Name: STOCKT
<br />Site
<br />CEON DF,aaS.t.rl !C:�t:4.�#'•�0083
<br />Site Address: 708U Zl�r✓.5 ;.�..'Tn•95 0
<br />�.�:• .',_.:��:��`;,idi y': L�:'+•
<br />STOCK
<br />°a ? G•° 'ra:;:f ir`.':'ss r.'.':r1.
<br />' is , 1\': r"' ��:': ':;r••.
<br />t , i..
<br />c ri'
<br />Date '4.Y':�i•i.me• o�..-ftii. M1e,s,t�.,f..,..:31'r1 °;..........
<br />No
<br />ks aifolded? n
<br />/fie the
<br />2 -PT
<br />operate)
<br />Total number OfT)077 coaxial
<br />Phase 1 vapor recovery system executive order (as referenced on Perrmt to Op BALANCE
<br />® 2, -point
<br />steal configuration it to O crate) 0 Phase 11 vapor riser
<br />Phase 1 vapor recovery .y � phase 1 vent line
<br />phase it vapor recovery system executive order (as referenced on erm ❑ niechamical gauge
<br />Phase i Vapor coupler — digital manometer 1/11/12
<br />',Nitrogen introduction point incline manometer sof the) 00
<br />pressure measuring device, within go
<br />Calibration date for pressure measuring device (m'� able (must be 0 O1 in. w'•c or less) 2 CFH.
<br />Ending value For digital mamm ter drift test if app 0
<br />F must b een 1 and 5 CPM j
<br />flow rate, ( e betty st be drained prior to testing) ,..,••,• q W.. Iti!N'T 'FY��' ji�cl��r�
<br />oduction ';I� a �;4 a,a,. �•�.-r .
<br />Nitrogen intr 10 (bal ce hoses mu 5"' w�� • �'"`I�fl :� ,��`..,i''r :. s ,, U
<br />pvEr 0 ml an ,. .,.... .. ;'• q�„ S . t(. .� y�h f'. '�'�'� �;c �f�!
<br />Number - . ,.,, . ,,,;:, � ,r,;, (�,.y.�y,�yl�,� .' -_ J ..... .,_..., .•.,c..�5x•Ndaiq.�'.Qi'rl�:'�?� itiV;f�;'v"dt r i • t .:�A ,,'�h'�.. r
<br />..,..,...,,,v+w.n.fn�µ'LV1,euw4�J�iJA',Y,�vl�r7dkA ."r- ti� 9 i '•4, d'
<br />, ""N
<br />ZZ�sa;n�;vr?;; yc ,,:ri, ;•, T. •...,•- $7
<br />�taynk
<br />�.,yl'6Produ4,000Actuapacity (gallons) 2,600
<br />Gasoline vo}u.mc (gallons) 400
<br />g (gallons)
<br />Ulla c (ga ) ].
<br />tanks are not. manifolded,
<br />number of nozzles
<br />1'f
<br />9�':lr iii �"�yR"'':,!'1�7u^-,','�'nilin;:;Y„'c: "',rjlv2'-,tr4'• - 0835
<br />Start timeN c) 2.00
<br />Initial Pressure, inches of water Column (in. 1.97
<br />Pressure at one minute, in w.c• 1 94
<br />Pressure at two minutes, in. w'c. 1.91
<br />Pressure at three minutes, T. w.c.
<br />1.88
<br />Pressure at four minutes, in. w.c.
<br />1.85
<br />PTcssure at five minutes, in' W.C. 1..16
<br />Allowable minimum pressure., i.n. w.c- PASS
<br />Pass ! Fail whichcwbe is �rermr-
<br />the te.t: shall be 25 ercent of the tank carmtitycor )QO gatlonc, r , r reasonable inytur)', the smlRments and
<br />I�OTF: 'The minimum ullage durinC ` P
<br />t dncfare, under penalty o(p�r%r�T under the !m�'< nf th!' 'Ttptc ojCafi(ornla tha ba.: d an injvrmatio � Ai'+d belie, formed � te'
<br />information Provided in rhtc document axe true, accurate. and cu?"PWC
<br />Signaturc of Technician:
<br />Date: 3123'12
<br />Z (7
<br />VED
<br />AIG227014
<br />"�NVIRONMErf7AL H
<br />D�P'AR ► t,V EALT1q
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