The figure shows the variation during startup of the torque absorbed by mechanical friction and imparted to the fluid.
The initial torque is due to mechanical friction, so the pump starting condition corresponds to left y axis. Approximately 15% of the torque.
At about 15-20% of full speed, the torque imparted to the fluid becomes the dominant component. Thereafter, the torque depends on the system head loss curve.
For a system dominated by static headloss, no flow occurs until the speed goes above the bottom curve of no flow.
The torque follows the bottom curve corresponding to shut off conditions of no flow.
As the pump speed increases, the flow increases rapidly as does the torque as it moves upward from the bottom curve.
With a zero static lift system, the flow begins to increase with less pump speed and torque.
For a system with higher static lift, the flow will not begin until the pump speed increases enough to surpass the static head (the bottom curve).
The actual vertical height is the static head that the slurry is to overcome. Variations in the vertical height (normally measured from the liquid level on the intake side of the pump to the discharge point or the high point in the line) can have a major effect on the output of any centrifugal pump. It is, therefore, important that this vertical height be determined within reasonable accuracy (1.5 ft.).