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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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Name of Supplier. Owner or Dealer <br />15. TANK TO TEST <br />Ua� L 4nO (J't H <br />Idenley, by pesiluon <br />Stand and Grade <br />17. FILL -UP FOR TEST <br />Stick Water Sonom <br />before Fill -up I -a in. <br />to <br />Address No. and StreNa) <br />15a. BRIEF DIAGRAM OF TANK FIELD <br />In. <br />0 Ilona Tank Diameter <br />18. SPECIAL CONDITIONS AND PROCEDURES TO TEST THIS T <br />Sae manual sections applicable. Check below and record procedure In log (27). <br />lbs maximum allowable test pressure for all testa. <br />Four pound rule does not apply to doublewalled tanks. <br />Complete section below: <br />1. Is four pound rule required? <br />2. Haight to 12- mark from bottom of tank <br />3. Pressure at bottom of tank <br />a. Prilfuta at top of tank <br />I of burial <br />dig. <br />table <br />NOTES: <br />Yes ❑ No ❑ <br />The above calculations are to be used for dry $all 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 />Well. <br />Rett to N.F.P.A. 30. Sectlons 212.4 and 2-7.2 and the tank <br />manufacturer regarding allowable system test pressures. <br />CM <br />16. CAPACITY <br />Nora" Capacity 10,000 <br />Gallons <br />By By most accurate �h. j �{ C t .l <br />capacity port wallabN <br />Gallons <br />Inventory <br />ANK ❑ Water In lank ❑ Llne(s) being leafed with LVLLT <br />❑ High water table M tank excavallon <br />19. TANK MEASUREMENTS FOR <br />TSTT ASSEMBLY <br />Bottom of tank to grade' ............................ �.js Irk <br />Add 30 - to! "r probe easy........ ................... 30 kl. <br />Total tubing to aseemble — approximate ............. In. <br />20. EXTENSION HOSE SETTING <br />Tank top to grade' .................................. In. <br />Extend nose on suction tube 6- of more <br />below tank top ................. I.................... In. <br />'lf Fill pipe extends above grade, use lop of fill. <br />22. Thermal -Sensor reading shot circulation <br />d ns <br />IF <br />�etwlaell <br />23. Digits per IF In range of expected change <br />dlgtts <br />COEFFICIENT OF EXPANSION (Complete after circulation) <br />24a. Corrected A.P.I. Gravity <br />Observed A.P.I. Gravity ................................... <br />State <br />Date 0 Tom <br />From <br />Station Chan <br />❑ Tank Manufacturer's Chan <br />❑ Company Engineering Data <br />❑ Charts supplied with <br />❑ pre« <br />Total Gallons <br />Gallons as. Reading ' <br />7;56 <br />Transfer foul to tans 254 <br />21. VAPOR RECOVERY SYSTEM ❑ stage I ❑ stage 11 <br />24b. COEFFICIENT OF EXPANSION <br />RECIPROCAL METHOD <br />Typ. of Product ........................... V 1�✓� r.� I = I� <br />Hydrometer Employed .................................. _les H <br />Temperature In Tank <br />Amer Circulation ........................................ t IF <br />Temperature of Sample ................................. ` w I n IF <br />Difference (•/-)......................................... /'y� IF <br />Observed A.P.I. Gravity ................................. Zia— <br />Reciprocal L' V `) Page a I..L <br />rL4 �' 40 <br />Total quantity M Reciprocal Volume change In <br />full tank (16 or 17) this lank per IF <br />Transfer to Line 26a, <br />Hydrometer employed ................................... H <br />, <br />Observed Sample Temperature ......................... •f 24c. FOR TESTING WITH WATER . Table C a o <br />Corrected A.P.I. Gravity Water Temperature Aur Circulation <br />LID6WF. From Table A .................................... Table C <br />Coefficient of Expansion Coefficient of Water <br />for involved Product Table D ................................................ <br />From Table S ....:....................................... <br />Transfer COE to Una 25b. Added Surfactant? ❑ Yes ❑ No Transfer COE to Line 25b. <br />25. (a) st (b) _ (c) ga6dn. <br />Total quantity N Coefficient of expamlon IN VAMO change In this tank <br />/hill''tank 1166 or 17) / Y vohM✓p��rod(u�cft� per •Fi\ ^ 1 CJ / I i <br />26. 11 0414 L y2 ♦ ._—� _ �J f"' r� 3 �( This Is <br />Yoiuune ,F r"+ as ?.akl -a• IF In Volume change per Agff ted <br />22. Thermal -Sensor reading shot circulation <br />d ns <br />IF <br />�etwlaell <br />23. Digits per IF In range of expected change <br />dlgtts <br />COEFFICIENT OF EXPANSION (Complete after circulation) <br />24a. Corrected A.P.I. Gravity <br />Observed A.P.I. Gravity ................................... <br />State <br />Date 0 Tom <br />From <br />Station Chan <br />❑ Tank Manufacturer's Chan <br />❑ Company Engineering Data <br />❑ Charts supplied with <br />❑ pre« <br />Total Gallons <br />Gallons as. Reading ' <br />7;56 <br />Transfer foul to tans 254 <br />21. VAPOR RECOVERY SYSTEM ❑ stage I ❑ stage 11 <br />24b. COEFFICIENT OF EXPANSION <br />RECIPROCAL METHOD <br />Typ. of Product ........................... V 1�✓� r.� I = I� <br />Hydrometer Employed .................................. _les H <br />Temperature In Tank <br />Amer Circulation ........................................ t IF <br />Temperature of Sample ................................. ` w I n IF <br />Difference (•/-)......................................... /'y� IF <br />Observed A.P.I. Gravity ................................. Zia— <br />Reciprocal L' V `) Page a I..L <br />rL4 �' 40 <br />Total quantity M Reciprocal Volume change In <br />full tank (16 or 17) this lank per IF <br />Transfer to Line 26a, <br />Hydrometer employed ................................... H <br />, <br />Observed Sample Temperature ......................... •f 24c. FOR TESTING WITH WATER . Table C a o <br />Corrected A.P.I. Gravity Water Temperature Aur Circulation <br />LID6WF. From Table A .................................... Table C <br />Coefficient of Expansion Coefficient of Water <br />for involved Product Table D ................................................ <br />From Table S ....:....................................... <br />Transfer COE to Una 25b. Added Surfactant? ❑ Yes ❑ No Transfer COE to Line 25b. <br />25. (a) st (b) _ (c) ga6dn. <br />Total quantity N Coefficient of expamlon IN VAMO change In this tank <br />/hill''tank 1166 or 17) / Y vohM✓p��rod(u�cft� per •Fi\ ^ 1 CJ / I i <br />26. 11 0414 L y2 ♦ ._—� _ �J f"' r� 3 �( This Is <br />Yoiuune ,F r"+ as ?.akl -a• IF In Volume change per Agff ted <br />Hydrometer employed ................................... H <br />, <br />Observed Sample Temperature ......................... •f 24c. FOR TESTING WITH WATER . Table C a o <br />Corrected A.P.I. Gravity Water Temperature Aur Circulation <br />LID6WF. From Table A .................................... Table C <br />Coefficient of Expansion Coefficient of Water <br />for involved Product Table D ................................................ <br />From Table S ....:....................................... <br />Transfer COE to Una 25b. Added Surfactant? ❑ Yes ❑ No Transfer COE to Line 25b. <br />25. (a) st (b) _ (c) ga6dn. <br />Total quantity N Coefficient of expamlon IN VAMO change In this tank <br />/hill''tank 1166 or 17) / Y vohM✓p��rod(u�cft� per •Fi\ ^ 1 CJ / I i <br />26. 11 0414 L y2 ♦ ._—� _ �J f"' r� 3 �( This Is <br />Yoiuune ,F r"+ as ?.akl -a• IF In Volume change per Agff ted <br />
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