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COMPLIANCE INFO 1986-2001
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2300 - Underground Storage Tank Program
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PR0231458
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COMPLIANCE INFO 1986-2001
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Last modified
12/29/2023 2:50:21 PM
Creation date
11/7/2018 1:12:28 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2300 - Underground Storage Tank Program
File Section
COMPLIANCE INFO
FileName_PostFix
1986-2001
RECORD_ID
PR0231458
PE
2361
FACILITY_ID
FA0001196
FACILITY_NAME
SAVE ON FUEL
STREET_NUMBER
420
Direction
W
STREET_NAME
YOSEMITE
STREET_TYPE
AVE
City
MANTECA
Zip
95337
APN
219-312-06
CURRENT_STATUS
01
SITE_LOCATION
420 W YOSEMITE AVE
P_LOCATION
04
P_DISTRICT
005
QC Status
Approved
Scanner
SJGOV\rtan
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\MIGRATIONS\IAError\Y\YOSEMITE\420\PR0231458\COMPLIANCE INFO 1986-2001.PDF
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EHD - Public
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' Diaphragm Model-No more than 1 to 3 oz.(about pump pressure.This indicates <br /> 1/2 cup), or 50 to 110 ml of that the LLD is opening prop- <br /> product should drain from the erly. <br /> line. If desired, RECORD opening <br /> ' Piston Model - No more than 11 to 14 oz.(about time in test chart. (See sample <br /> 1-1/2 cups),or 350 to 410 ml of test chart on Page 8.) <br /> product should drain from the * This is the point at which the LLD is in the leak <br /> ' line. <br /> * Leave the valve open for approximately 60-90 sensing(metering) position- step 2 of the 3 step <br /> seconds after zero line pressure is obtained. test shown on pp. 6 and 7. <br /> This allows the piston to reset. <br /> ' If larger amounts of product are measured,it is SIMULATED LEAK TEST <br /> possible air is still present in the system. 5. A simulated leak can be placed on the system by <br /> First turning off the submersible pump, fully <br /> ' III. OBSERVATION OF LEAK DETECTOR opening the ball valve to drop pressure to zero. <br /> OPENING TIME For piston model LLD's, experi- <br /> 4. Next,close the valve and start the submersible ence has shown that if product is <br /> pump for: still drippingfrom the discharge <br /> Diaphragm Model -The line pressure should rise hose after approximately one <br /> to approximately 8 to 12 psi minute,usually within the next <br /> immediately*. On a current 60 seconds, a small stream of <br /> i style diaphragm LLD,the line fluid will spurt out. This is an <br /> pressure should then rise to indication that the leak detector <br /> full pump pressure, 26 to 30 has dropped into the leak sens- / <br /> ' psi,in approximately two sec- ing position. l <br /> onds. (On the old style it will With the ball valve fully open to allow a leak <br /> take five seconds.)Because rate,Restart the submersible pump leaving the <br /> flow is allowed into the dis- dispenser nozzle closed.Depending on the size <br /> '. charge line by the leak detec- of the leak through the ball valve,the pressure <br /> for when approximately 12 psi gauge may read from 0 to 13 psi for diaphragm <br /> is realized under the dia- models,or from 0 to 22 psi for piston models. <br /> phragm(this takes the poppet 6. Throttle down the flow rate through the ball <br /> to Position 3 on the 3-step leak <br /> test), you probably will not valve until the simulated leak is at the desir- <br /> ' detect a pause on the pressure able rate. See chart below. <br /> gauge at the 12 psi positionbut Leak Rate Conversion Chart <br /> will see a jump from approxi- DIAPHRAGM DIAPHRAGM PISTON PISTON <br /> ' mately 8 psi to full pump pres- GPH IN OZIMIN CUMIN 0VMIN <br /> sure (approximately 26 to 30 1 63 2.13 93.44 3.16 <br /> psi,depending upon the horse- 2 126 4.26 186.88 6.32 <br /> ' power of the pump motor) in 3 189 6.40 280.33 9.48 <br /> the prescribed time.This indi- 4 252 8.50 373.77 12.64 <br /> cates that the leak detector is 5 315 10.70 467.22 15.80 <br /> operating properly. 6 378 12.80 560.66 18.96 <br /> ' Piston Model - The line pressure should rise 7 441 14.90 654.10 22.12 <br /> to approximately 17 to 22 psi 8 504 17.10 747.55 25.28 <br /> immediately.The linepressure 9 567 19.20 840.99 28.44 <br /> ' should then rise to full pump 10 630 21.30 934.44 31.60 <br /> pressure, 26 to 30 psi, in ap- <br /> proximately two seconds.You NffTr.TffM The above are calculated flows <br /> 1 may notice a slight dip in pres- on a typical Ml valve and are for <br /> sure on the pressure gauge at referenceonly.Actualflowsmay <br /> approximately 17 to 22 psi* vary from valve to valve. <br /> then an immediatejump to full The dispenser nozzle can now be opened and the <br /> ' 4 <br />
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