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4-2 HANDBOOK OF HYDRAULICS <br />approximately diameter downstream from the inner face of <br />the orifice plate. The area at the vena contracts, as in Fig. <br />4 -1, is related to the area of the orifice a as follows: <br />as '" C.a (4-1) <br />where C. is called the coefficient of contraction. <br />The contraction is caused by the fact that those elements of <br />the fluid with approach from the aide of the orifice have trans- <br />verse velocity components directed <br />toward the center of the orifice. <br />Therefore the nearness of bounda- <br />ries, as, for example, for orifices in <br />pipes (p. 4 -14), would tend to reduce <br />the amount of contraction and <br />increase C.. If one edge of an <br />orifice is flush with a wall, the con- <br />traction on that side will be entirely <br />eliminated. However, the con- <br />traction from the other side will <br />be increased by approximately <br />the same amount. Increasing the <br />roughness of the inner face of the <br />orifice plate would also reduce the <br />transverse velocity components <br />slightly. Rounding the inner edge <br />of the orifice reduces contraction, <br />and the contraction can be eliminated completely by shaping the <br />orifice to conform with the form of the contracting jet as shown <br />in Fig. 4-2. <br />Fundamental Equations. The Bernoulli equation (Sec. 3), <br />written from any point in the liquid, such as 1 in Fig. 4-1, to the <br />vena contracta (point 2), taking the datum plane through the <br />center of the orifice, is <br />Fro. 4-2. Bell- mouthed <br />orifice with rounded up- <br />stream edge. <br />and <br />vs <br />VII Or V: VI <br />2g w 2g w <br />(4-2) <br />`w w 2g <br />Point 2 being located where the jet has ceased to contract, its <br />pressure is that of the surrounding fluid. For discharge into <br />(4 -3) <br />ORIFICES, GATES, AND TUBES 4-3 <br />the atmosphere, ps is therefore zero on the gage scale. For large <br />tanks, v, is so small that it may be neglected. Replacing pl/w <br />with h and dropping the subscript of vs, Eq. (4-3) may now be <br />written <br />v m V2g0 — h,) (4-4) <br />Neglecting energy losses, the equation for the theoretical <br />velocity becomes <br />(4-8) <br />(4-6) <br />or <br />Then <br />h <br />C l , ffi g <br />The expression v,'/2g is termed the velocity head. Table <br />4-1 gives values of v, for heads from 0 to 50 ft, and Table 4-2 <br />gives h. for velocities from 0 to 50 ft per see. <br />It is convenient to take care of the energy loss by introducing <br />a coefficient of velocity C.. Thus, instead of subtracting the <br />energy loss as in Eq. (4-4), the expression for the velocity at the <br />yens contracts may be written <br />v m C. (4 -7) <br />The discharge is the product of the velocity and area at the <br />vena contracta as follows: <br />Q m alas ( <br />Inserting the value of a from Eq. (4-1) and the value of v <br />from Eq. (4-7), <br />Q - CAC. ViTh (4-9) <br />The product of the coefficient of velocity C, and the coefficient <br />of contraction C. is called the coefficient of discharge C. Equa- <br />tion (4 -9) may then be written <br />Q m Ca 1,r2g7i (410) <br />The energy lose may be expressed in terms of C. by equating <br />the expressions for v given in Eqs. (4-4) and (4-7) as follows: <br />V2g(h hr) °° C, 1/ <br />hr a (1 -- C.')h (4 -11) <br />