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component to an otherwise "passive" system and <br />add cost because of the dosing equipment. The <br />improved performance of dosed -flow systems over <br />gravity flow systems should outweigh these perceived <br />disadvantages, especially when a management <br />entity is in place. It must be noted, however, that if <br />dosed infiltration systems are allowed to pond, the <br />advantages of dosing are lost because the bottom <br />infiltration surface is continuously inundated and <br />no longer allowed to rest and reaerate. Therefore, <br />there is no value in using dosed -flow distribution in <br />SWISs designed to operate ponded, such as systems <br />that include sidewall area as an active infiltration <br />surface or those using serial relief lines. <br />Perforated pipe <br />Four -inch perforated pipe networks (with or <br />without d -boxes or pressure manifolds) that receive <br />dosed -flow applications are designed no differently <br />than gravity -flow systems. Many of the advantages <br />of dosing are lost in such networks, however, <br />because the distribution is only slightly better than <br />that of gravity -flow systems (Converse, 1974). <br />Pressure manifold <br />A pressure manifold consists of a large -diameter <br />pipe tapped with small outlet pipes that discharge <br />to gravity laterals (figure 4-14). A pump pressur- <br />izes the manifold, which has a selected diameter to <br />ensure that pressure inside the manifold is the same <br />at each outlet. This method of flow division is <br />more accurate and consistent than a distribution <br />box, but it has the same shortcoming since flow <br />after the manifold is by gravity along each distribu- <br />Figure 4-14. Pressure manifold detail <br />Inlet pipe <br />tion lateral. Its most common application is to <br />divide flow among multiple trenches constructed at <br />different elevations on a sloping site. <br />Table 4-7 can be used to size a pressure manifold <br />for different applications (see sidebar). This table was <br />developed by Berkowitz (1985) to size the manifold <br />diameter based on the spacing between pressure lateral <br />taps, the lateral tap diameter, and the number of <br />lateral taps. The hydraulic computations made to <br />develop the table set a maximum flow differential <br />between laterals of 5 percent. The dosing rate is <br />determined by calculating the flow in a single lateral <br />tap assuming 1 to 4 feet of head at the manifold <br />outlets and multiplying the result by the number of <br />lateral taps. The Hazen -Williams equation for pipe <br />flow can be used to make this calculation. <br />Pressure distribution is typically constructed of <br />Schedule 40 PVC pipe (figure 4-15). The lateral <br />taps are joined by tees. They also can be attached <br />by tapping (threading) the manifold pipe, but the <br />manifold pipe must be Schedule 80 to provide a <br />thicker pipe wall for successful tapping. Valves on <br />each pressure tap are recommended to enable each <br />line to be taken out of service as needed by closing <br />the appropriate valve. This allows an opportunity <br />to manage, rest, or repair individual lines. To <br />prevent freezing, the manifold can be drained back <br />to the dose tank after each dose. If this is done, the <br />volume of water that will drain from the manifold <br />and forcemain must be added to the dose volume to <br />achieve the desired dose. <br />Rigid pipe pressure network <br />Rigid pipe pressure distribution networks are used <br />to provide relatively uniform distribution of <br />Enlargers to increase pipe <br />Distribution laterals to size of trench pipe <br />4-24 USEPA Onsite Wastewater Treatment Systems Manual <br />