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INSTALL 1994 PIPING
Environmental Health - Public
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2300 - Underground Storage Tank Program
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PR0231948
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INSTALL 1994 PIPING
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Last modified
1/18/2022 4:58:51 PM
Creation date
4/26/2019 2:34:17 PM
Metadata
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Template:
EHD - Public
ProgramCode
2300 - Underground Storage Tank Program
File Section
INSTALL
FileName_PostFix
1994 PIPING
RECORD_ID
PR0231948
PE
2361
FACILITY_ID
FA0003855
FACILITY_NAME
TESORO (SHELL) 68153
STREET_NUMBER
2448
Direction
W
STREET_NAME
KETTLEMAN
STREET_TYPE
LN
City
LODI
Zip
95240
APN
05814001
CURRENT_STATUS
01
SITE_LOCATION
2448 W KETTLEMAN LN
P_LOCATION
02
P_DISTRICT
004
QC Status
Approved
Scanner
KBlackwell
Tags
EHD - Public
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THE XLP. . .3 STEP LEAK TEST <br /> The Red Jacket XLP leak detector is hour) is metered through the XLP into flow to approximately 1-1/2 to 3 GPM. <br /> a pressure-sensing, piston-operated the piping system. ff a leak is present This is the indication to the operator that <br /> valve designed to indicate a leak in the that equals or exceeds this amount,as a leak is present.' C <br /> piping between the leak detector and much product escapes from the system H there are no leaks, pressure rapidlybuilds in the system forcing the XLP to <br /> the dispenser. as is metered in through the XLP. open to the full-flow position. In a <br /> When the line pressure is at approxi- Under this condition pressure cannot system with no leaks, it takes approxi- <br /> mately less than 1 psi and the sub- build up in the piping system. When a mately two seconds for a complete test. <br /> merged pump is turned on, a controlled nozzle is opened, a poppet in the XLP No further line testing takes place until <br /> amount of product (three gallons per moves to a position that restricts the the line pressure drops below 1 psi. <br /> Or <br /> 0 <br /> Position 1 Position 2 <br /> Position 3 <br /> Vented Vented Vented <br /> to Tank to Tank I to Tank <br /> Pressure Relief 20-22 PSI <br /> Valve <br /> Lessthan <br /> 1 PSI <br /> \ Full Pressure \ Full Pressure Full Pressure <br /> Poppet Approx.25 PSI Approx.25 PSI � Approx,25 PSI <br /> E—from Pump �. t—from Pum �, E—from Pum <br /> Metering Pin <br /> Less than A, 20 to 22 PSI,, A�V �� All Pressure A- <br /> ��' 1 PSI - Equal <br /> IT.Discharge Line ITo Discharge Line . To Discharge Line <br /> 1. The Trip or Relaxed Position. Under 2. Leak Sensing Position. As the If there is no leakage in the system, the <br /> normal operating conditions, it is pressure builds to approximately 20 to 22 small flow around the metering pin <br /> assumed that the lines are filled with psi (rapidly)the piston has moved the increases the line pressure to 22 psi in <br /> gasoline. When the system pressure is poppet to such a position as to almost approximately two seconds at which <br /> less than 1 psi, the piston and poppet are stop the flow into the piping through the point the piston will snap the poppet to <br /> in their'down'or-tripped-position. The XLP valve poppet. In this position,all Position 3,allowing full flow. Any product <br /> position of the valve poppet is such as to the flow must then travel around the relieved through pressure relief valve <br /> allow approximately 1-1/2 to 3 GPM flow metering pin which limits it to approxi- during trip position will be vented through <br /> into the delivery line through a bypass mately 3 GPH rate. If a simultaneous vent tube to tank. This allows piston to <br /> opening in the XLP valve poppet when loss from the system equals or exceeds move freely with no back pressure to <br /> the submersible pump starts. Since the this amount, the line pressure will not hamper its movement. <br /> system is full, pressure builds rapidly and build beyond this point and the valve will 3. Non-Leak Position. This position allows <br /> the poppet moves to the leak sensing remain in the leak sensing position with full flow. The poppet will remain in this <br /> position assuming there is no leak the main flow blocked. If there is an position as long as the sytem pressure <br /> present. The pressure relief valve attempt to dispense while the valve is in remains above 1 psi. At less than 1 psi, <br /> prevents any build up of pressure under this position, the line pressure will drop, the poppet will return to Position 1 and <br /> piston when in trip position by allowing the piston will respond,and the poppet the next time the pump is activated, the <br /> relief of trapped product. will return to Position 1 where the 1-1/2 XLP will perform a line test. <br /> to 3 GPM will flow to the dispensers.' <br /> 'If the dispensing system (the solenoid valve and the nozzle)is opened previous to the completion of the line test,the XLP will detect this opening <br /> as a leak and restricted flow will result. Closing of the nozzle(s) for a period of time, adequate to allow completion of the line test,will allow the XLP <br /> to open. This, in turn,will allow full flow providing there is no additional escape for fuel in the system. <br /> k7,17rtMThis product is designed and sold to detect leaks of approximately 3GPH or greater only. For leaks <br /> of less than approximately 3GPH, please consult with your Marley Pump Company representative. <br /> XLP-31" 3/91 "MARLEY <br />
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