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v <br />Component <br />Test Method <br />Starildard or,Specification <br />Husky <br />Pressure/Vacuum Vent Valve <br />Minimum, 360 -degree rotation <br />Rotatable Phase I <br />TP -201.1 B <br />Maximum, 108 pound -inch average static <br />Adaptors <br />Pressure/Vacuum Vent Valve <br />torque <br />Overfill Prevention <br />TP -201.1 D <br /><_0.17 CFH at 2:00 in. H2O <br />Device <br />61-T Straight Drop Tube <br />Annual <br />Spill Container Drain <br />TP -201.1 C or <br />17 CFH at 2.00 in. H2O <br />Valve <br />TP -201.1 D <br />_<0. <br />OPW <br />Drop Tube Overfill Prevention Valve <br />Positive pressure setting: 3.0 ± 0.5 in. H2O <br />P/V Valve' <br />TP -201.1 E <br />Negative pressure setting: -8.0 ± 2.0 in. H2O <br />Positive Leakrate: 0.05 CFH at 2.0 in. H2O <br />Ne ative Leakrate: 0.21 CFH at -4.0 in. H2O <br />Gasoline Dispensing <br />TP -201.3 <br />As specified in TP -201.3 and/or CP -201 <br />Facility <br />Connections and fittings <br />Leak <br />Detection <br />certified without an <br />Solution or <br />No leaks <br />allowable leak rate <br />Bagging <br />Table 2-2 <br />Maintenance Intervals for System Components <br />Manufactwrer <br />Component <br />Maintenance Interval <br />Husky <br />Pressure/Vacuum Vent Valve <br />Annual <br />Morrison Brothers <br />Tank Gauge Components <br />Annual <br />OPW <br />Pressure/Vacuum Vent Valve <br />Annual <br />OPW <br />Dust Caps (all models) <br />Annual <br />OPW <br />61-T Straight Drop Tube <br />Annual <br />OPW <br />Ball Float (all models) <br />Every 3 years <br />OPW <br />Rotatable Phase I Adaptors <br />Annual <br />OPW <br />Drop Tube Overfill Prevention Valve <br />Annual <br />OPW\Pomeco <br />Spill Containers (all models) <br />Annual <br />1, Compliance determination is at the option of the district. <br />Executive Order VR -102-E, OPW Phase I Vapor Recovery System, Exhibit 2, Page 5 <br />