Page 93 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 93
Fluid Flow 79
4 y 5 0
K, = 0.016 K, = 0.034 K, = 0.042 K, = 0.066 K, = 0.130 K, = 0.236
K, = 0.024 K, = 0.044 K, = 0.062 K, = 0.1 54 K, = 0.1 65 K. = 0.320
K, = 0.400
, = 0.112 K, = 0.323 K, = 0.601
= 0.284
"OPTIMUM VALUE OF a INTERPOLATED
K, = RESISTANCE COEFFICIENT FOR SMOOTH SURFACE
IC, = RESISTANCE GOEFFICIENT FOR ROUGH SURFACE, -1. sz 0.0022
D
Figure 2-14. Resistance coefficients for miter bends at Reynolds number = 2.25 x 1 O5 for water. Reprinted by permission, Hydraulic Institute
Engineering Data Book, .I st Ed., 1979, Cleveland, Ohio.
1.0 1.5 2.0 2.5 3.0 3.5 4.0
ESISTANCE COEFFICIENTS FOR REDUCERS
Figure 2-65. Resistance coefficients for reducers for water. Reprinted by permission, Hydraulic Institute, Engineering Data
Cleveland, Ohio,
