Page 146 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 146
130 Applied Process Design for Chemical and Petrochemical Plants
STANDARDS OF THE HEAT EXCHANGE INSTITUTE, INC.
1000
800
600
400
200
""'
<,J
a:
;=,
E- 100
<
a:
<,J 80
Cl.
::; 60
<,J
E-
40
1.0 1.4 1.8 2.2 2.6 3.0 3.4 3.8 4.2 4.6 5.0
CrC'.,. TEMPERATURE CORRECTION FACTORS
60
40
u:
<,J
:r:
u 20
�
0::
<,J
E-
<,J 10
::;;
<
s 8
<,J 6
Cl.
5::
..J
-e 4
;=,
E-
u
-e
2
10-• IO__. 10-• 10- 1 10--'
Note: friction Factors FI and F 2 are based on rate of flow, while Factors Co I and Co2 are based on actual pipe diameter.
Figure 2-43. Evaluation curves for friction losses of air and steam flowing turbulently in commercial pipe at low pressures. By permission,
Standards for Steam Jet Ejectors, 4th Ed., Heat Exchange Institute, 1988.
