Case: Operating point for a pump: 

If pump characteristic curve is given for a pump, and it is required to obtain an operating point, then the system-head curve need to be constructed as follows:

 

 

Where c is a considered to be fairly independent of capacity Q.  In a system with gravity head (negative lift) fluid flow will continue until the system friction loss equals the available gravity head.  The point of intersection, A, between the H-Q and system curves is the operating point of the pump.  When pipes of different sizes are used, the system head curve shifts in such a way that "higher head" can be obtained for a smaller diameter for same capacity Q.

 

Example 4.21: Two reservoirs are connected with a long pipe which has characteristics such that the head loss through the pipe is expressed as hfs = 0.002 Q2, where hfs is in ft·lbf/lb and Q is the flow rate in gpm.  The water surface elevation in reservoir B is 35 feet above that in reservoir A.  Two identical pumps are available to pump the water from A to B.  The characteristic curve of the pump when operating at 1800 rpm is given below:

 

 

Ha/ft

 

100

 

90

 

80

 

60

 

40

 

20

 

Qa/gpm

 

0

 

110

 

180

 

250

 

300

 

340

 


Find the rate of flow under the following operating conditions:  a) single pump; b) two pumps in series; and c) two pumps in parallel, each operating at 1800 rpm.

 

Solution:  Total static head = 35 feet, Frictional head = 0.002 Q2.  System curve is given as

 

 

Draw a system head (h-Q) curve.  Intersection of system head-curve and pump head-capacity (Ha-Qa) curve can be seen to occur at 156 gpm at a head of 83.6 ft.

 

If another pump is added in series, then head H is to be doubled for given Q.  The pump-head capacity (Hb-Qb) curve will be

 

 

Hb/ft

 

200

 

180

 

160

 

120

 

80

 

40

 

Qb/gpm

 

0

 

110

 

180

 

250

 

300

 

340

 

This system curve does not change.  Now the intersection of the pump-head capacity (Hb-Qb) curve and the system curve can be found to be at 224 gpm and 135.4 ft.

 

If a pump is added in parallel, then new Q is twice the original value for a given H.

 

Hc/ft

 

100

 

90

 

80

 

60

 

40

 

20

 

Qc/gpm

 

0

 

220

 

360

 

500

 

600

 

680

 

Now the intersection of the pump-head capacity (Hc-Qc) curve and the system curve can be found to be at 170 gpm and 92.8 ft.  The intersection of Ha, Hb, and Hc curves with the system curve h occurs at 156 gpm, 224 gpm, and 170 gpm, respectively.