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COMPLIANCE INFO_1985-1998
Environmental Health - Public
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2300 - Underground Storage Tank Program
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PR0231342
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COMPLIANCE INFO_1985-1998
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Last modified
11/4/2021 2:57:00 PM
Creation date
6/3/2020 9:46:52 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2300 - Underground Storage Tank Program
File Section
COMPLIANCE INFO
FileName_PostFix
1985-1998
RECORD_ID
PR0231342
PE
2361
FACILITY_ID
FA0000392
FACILITY_NAME
FLAMES LIQUOR
STREET_NUMBER
1301
Direction
W
STREET_NAME
KETTLEMAN
STREET_TYPE
LN
City
LODI
Zip
95242
APN
03104030
CURRENT_STATUS
01
SITE_LOCATION
1301 W KETTLEMAN LN
P_LOCATION
02
P_DISTRICT
004
QC Status
Approved
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SJGOV\rtan
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\MIGRATIONS\UST\UST_2361_PR0231342_1301 W KETTLEMAN_1985-1998.tif
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EHD - Public
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14. FLAME LIQUOR 1301 WEST KETTLEMAN LANE LODI, CALIF. 95240 <br />Name of Supplier. Owner or Malar Address No. and Sit"($) <br />15. TANK TO TEST <br />C✓,= fir �G� <br />fdenidyby position <br />1el',�We, W <br />Brand and Grade <br />17. FILL -UP FOR TEST <br />Suck Water Bottom <br />before Fill -up <br />to u^ <br />I <br />City <br />15a. BRIEF DIAGRAM OF TANK FIELD 16. CAPACITY . <br />Nominal Capacity <br />Gallons <br />Gallons <br />18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS TANK <br />See manual sections applicable. Check below and record procedure In log (27). <br />Use maximum allowable lest pressure for all tells. <br />Four pound rule does not apply to doublewalled tanks. <br />Complete section below; <br />1. is four pound rule required? <br />2. Height a i r mark from gree. <br />3. Pressure at bottom of tank <br />4. Pressure at top of tank <br />M010"12-41 <br />3G in. <br />( q 72 <br />P.S.I. <br />G r `tel/ G•-- P.S.I. <br />h of burial - 7` In. <br />dim. In. <br />rr table to tank Dolton <br />NOTES: <br />The above calculations are to be used for dry soil conditions to <br />establish a positive pressure advantage, or when using the four pound <br />rule to compensate for the presence of subsurface water in the tank <br />area. <br />Refer to N.F.P.A. 30. Sections 2-3.2.4 and 2.7.2 and the tank <br />manufacturer regarding allowable system lett pressures. <br />most accurate e r// �U <br />capacity CMA available < !!! ��(JJJ <br />Gallons <br />in. <br />Tank Dismoter <br />❑ Water In tank ® Line(s) being tested with LVLLT <br />❑ Nigh water table In tank excavation <br />19. TANK MEASUREMENTS FOR <br />TSTT ASSEMBLY G <br />Bottom of tank to grade ............................. In. <br />Add30^ for i probe usy........................... 7 30 In. <br />Total tubing to assemble — approximate ............. ` � In. <br />20. EXTENSION HOSE SETTING <br />Tank top to grade' .................................. In. <br />Extend hose on auction tube e- or more <br />below tank top ...................................... In. <br />'If Fill pipe extends above grade, use top of fill. <br />USE WITH THERMAL SENSOR <br />PN5039 (Blue Bax) <br />22. Thermal -Sensor reading after circulation <br />digits <br />.F <br />Between <br />23. Digits per IF In tongs of expected change <br />a. IF USING THERMAL SENSOR OTS -2000 <br />OR OC -2000 WHICH READ 1000 DIGITS <br />PER OF TRANSFER 1000 TO LINE 26, <br />DIGITS PER OF IN TEST RANGE. <br />767 <br />,17e <br />Stale <br />-/s.-,�z <br />Date of Tat <br />From <br />Total Gallons <br />® <br />Station Chart <br />❑ <br />, <br />Water Bottom <br />Tank Manufacturer's Chart <br />❑ <br />Company Engineering Data <br />❑ <br />Charts supplied with Tank Testa <br />❑ <br />•F <br />Temperature of Samplo................................. <br />Other <br />24b. COEFFICIENT OF EXPANSION <br />Total Gallons <br />RECIPROCAL METHOD <br />ea. Heading <br />Inventory In Tank <br />, <br />Water Bottom <br />`r H <br />Top oft equipment <br />$ <br />( ,✓ <br />Total Ouanlity <br />77 t <br />21. VAPOR RECOVERY SYSTEM Z Stage 1 ® stage if <br />24b. COEFFICIENT OF EXPANSION <br />x (b) _ <br />RECIPROCAL METHOD <br />gallons <br />.............................. <br />Type of Product.......... <br />Hydrometer Employed .................................. <br />`r H <br />Temperature In Tank <br />Involved product <br />��(1V <br />After Circulation ........................................ <br />IF <br />26. _ <br />Volume change per IF 125 or lob) <br />•F <br />Temperature of Samplo................................. <br />�� <br />/�/% <br />Difference (•/-) .................................... <br />j,6 <br />Observed A.P.I. Gravity ................................. <br />`Gr Page a "� O <br />/ <br />Reciprocal <br />994?6 , <br />6,W7 ,7Z7 <br />Total quantity In Reciprocal <br />full tank (17) <br />Volume change In <br />this tank per IF <br />Transfer to Line ties, <br />24c. FOR TESTING WITH WATER see Table C a o <br />Water Temperature after Circulation <br />Table C from Thermal Sensor ............................ •F <br />Coefficient of Water <br />Table D ................................................ <br />Added Surfactant? ❑ Yoe ❑ No Transfer COE to Line 25b. <br />25. (a) <br />x (b) _ <br />(c) <br />gallons <br />Total quantity in <br />Cosfltolont of expansion for <br />Volume change In this tank <br />full tank (17) �J �j �f' '% <br />(a) t�os �L 7Z7 < <br />Involved product <br />��(1V <br />per IF /-fir 7 <br />� �0IP IL 70 <br />This Is <br />26. _ <br />Volume change per IF 125 or lob) <br />e <br />Digits per IF in tut <br />Volume change per digitbal <br />�� <br />Range (23 or 24s) <br />Compute to 4 decimal places. <br />factor (a) <br />
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