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41. <br />b. The positive pressure setting is 3.0 ± 0.5 inches of H2O and the negative <br />pressure setting is -8.0 ± 2.0 inches of H2O as determined by TP -201.1 E, <br />Leak Rate and Cracking Pressure of PressureAlacuum Vent Valves. <br />3. A manifold may be installed on the vent pipes to reduce the number of potential <br />leak sources and PN valves installed. Vent pipe manifolds shall be constructed of <br />steel pipe or an equivalent material that has been listed for use with gasoline. If a <br />material other than steel is used, the GDF operator shall make available, <br />information demonstrating that the material is compatible for use with gasoline. <br />One example of a typical vent pipe manifold is shown in Figure 2D. This shows <br />only one typical configuration; other manifold configurations may be used. For <br />example, a tee may be located in a different position, or fewer pipes may be <br />connected, or more than one PN valve may be installed on the manifold. <br />4. The vent pipe manifold shall be installed at a height not less than 12 feet above the <br />grade used for gasoline cargo tank delivery operations and shall conform to all <br />applicable regulations. <br />5. Each PN valve shall have permanently affixed to it a yellow or gold -colored label <br />with black lettering stating the following specifications: <br />Positive pressure setting: 3.0 ± 0.5 inches H2O <br />Negative pressure setting: -8.0 ± 2.0 inches H2O <br />Positive Leakrate: 0.05 CFH at 2.0 inches H2O <br />Negative Leakrate: 0.21 CFH at -4.0 inches H2O <br />1:n* F1M1'1rMTMMqF.r1r6M '. <br />Rotatable product and vapor recovery adaptors shall be capable of at least <br />360 -degree rotation and have an average static torque not to exceed 108 pound - <br />inch (9 pound -foot). Compliance with this requirement shall be demonstrated in <br />accordance with the latest adopted version of TP -201.1 B, Static Torque of <br />Rotatable Phase I Adaptors. <br />2. The vapor adaptor poppet shall not leak when closed. Compliance with this <br />requirement may be verified by the use of commercial liquid leak detection solution <br />or by bagging, when the vapor containment space of the underground storage tank <br />is subjected to a non -zero gauge pressure. (Note: leak detection solution will <br />detect leaks only when positive gauge pressure exists.) <br />Dust caps with intact gaskets shall be installed on all Phase I tank adaptors. <br />Executive Order VR -102-E, OPW Phase I Vapor Recovery System, Exhibit 2, Page 2 <br />