Page 152 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

138 Applied Process Design for Chemical and Petrochemical Plants

4 1.200~ -.I677 { v2 } -.6938
J
t2 =r f W O D(s-119
2-

10-2:-
8-
-
6-
-
4-
f -fw=.
2-

10-3:-
8-
-
6-
-
4-

2-
3:
CF
lo-+-
8-
-
6-
4-
-

2- n

8- 3
-
6- t
-
4-

IO+ ! I I I I I Ill1 I I I I IF111 I I I I I1111 I I I l l l ~

10-5 2 4 6 810-4 2 4 6 810-3 2 4 6 2 4 6 SI
t2.
Figure 2-51. Friction factor correlation for slurry flow in heterogeneous flow regime. By permission, Turian, R. M. and Yuan, T. F., “Flow of Slur-
ries in Pipelines,” A. /.Ch.€. Journal, vol. 23, 1977, p. 232-243.

12. Refer to the large pipe multipliers shown in the 13. Calculation of “factor scale” for receiver pressures
table on the chart, and select the pipe size whose different than those shown on chart:
factor is equal to or smaller than the result of step
(11) above. This is the pipe size to use, provided a
sufficient factor of safety has been incorporated in factor = 36.2 (v) (h - h ) (2 - 134)
the data used for the selection of pipe size. Ly (hp - 180)