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��'�'ITA�4A7'H7-�913C�[lJEI4'" <br /> �din�YYfp Cwpry <br /> Other possible leak scenarios include a leak developing in the siphon bar, developing in the <br /> fuel supply line to the fuel island dispensers, or fuel siphoning out of the tank through the <br /> fuel supply line. Safeguards for each of these modes is described below. <br /> The siphon bar is a 2" diameter pipe that runs from near the bottom of one tank, up and <br /> over to the other tank, and down to near the bottom of the other tank. For the siphon to <br /> work, it must be full of fuel. If it develops a leak, air will enter the siphon bar and break the <br /> siphon. Only a small quantity spill would be expected from this scenario. <br /> If a leak developed in the fuel supply line, product might siphon out from the tank into the <br /> curb/bermed area. However,the fuel supply pump is equipped with an anti-siphon <br /> solenoid valve. <br /> As discussed on the Petroleum Equipment Institute website <br /> (https://www.pei.org/wiki/antisiphon-valve): <br /> On systems where the piping connections come out of the top of an AST it consists of a <br /> small normally open solenoid valve which is installed in the highest point in the pipe run. It <br /> is de-energized (open) when the pump is not running. Loss of prime back into the tank is <br /> prevented by installing a check valve in the suction riser pipe coming up out of the tank. <br /> When the pump is turned on,the solenoid is energized, and it closes. Normal pump suction <br /> draws fuel up out of the tank, and down to the pump.When the pump is shut off the <br /> solenoid (siphon breaker) opens again. If there is a leak, or a valve in the pump or <br /> downstream of the pump is accidentally left open, or of a pump seal fails, fuel will flow out <br /> of the system, but with the siphon breaker introducing air into the piping as fuel flows out, <br /> only the amount of fuel held in the pipe will spill out. None will be drawn out of the tank by <br /> siphon, because the siphon breaker has introduced air into the suction line and broken the <br /> continuous siphon effect. <br /> Oil-filled Operational Equipment <br /> Oil-filled operational equipment at this facility, (i.e., electrical transformers), does not have <br /> passive secondary containment. Active containment measures are used to prevent a <br /> release from reaching navigable waters. A Spill Control Equipment supplies drum is <br /> located near each of the three transformers. <br /> The typical failure mode, and the most likely quantity of oil that would be discharged from <br /> a leaking transformer are as follows: <br /> • A spill from maintenance of the transformer dielectric fluid <br /> • A release due to a hole in the dielectric fluid reservoir or cooling fins <br /> • The release rate is not expected to be greater than 6 gpm, except in the instance of a <br /> transformer fire. This rate is estimated by calculating the flow rate through a 1/2" <br /> diameter hole (puncture) with 4 ft of head (full transformer). The release rate <br /> would decrease as the height of the dielectric fluid dropped. <br /> Secondary Containment Calculations Page 2 of 5 Appendix L <br />