Page 235 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 235
Pumping of Liquids 205
l.00
.90
.80 §
en .70.
Q: �-
.60
�
z .50
0
j::
(.) .40
l&I
Q: Reproduced with permission of
Q:
8 .30 INGERSOLL-RAND COMPANY .
. 20
.10
b
.,(fl
?,(fl
,tfl
.... .,o.
'\.(fl
t:i ¥P
... ffJ
l&I
� t,O
Q ?,0
<
l&I
::c ,f)
'-"
'\.o
ii
b
I
10 15 20 25 30 50 60 70 80 90 100
CAPACITY-GALLONS PER MINUTE (at bep)
Figure 3-57. Viscosity performance correction chart for small centrifugal pumps with capacity at best efficiency point of less than 100 GPM
(water performance). Note: Do not extrapolate. For small centrifugal pumps only, not for axial or mixed flow. NPSH must be adequate. For
Newtonian fluids only. For multistage pumps, use head per stage. (By permission, Hydraulic Institute Standards for Centrifugal, Rotary, and
Reciprocating Pumps, 13th ed., Hydraulic Institute, 1975.)

