Vertical Turbine Pumps

 

Pump lift is an adjustment procedure generally associated with vertical, mixed flow type pumps. These pumps also go by the descriptors vertical turbine pumps, irrigation pumps, barrel pumps, fire pumps, or propeller pumps.

 

In general, this type of pump takes water from a reservoir and pumps it vertically through a riser, called a flow tube, to a higher elevation. The flow tube also contains the shaft which connects the motor which is located on top to the pump impeller which is immersed in the reservoir. Water from the reservoir enters the impeller axially at the bottom of the pump and is discharged both axially and radially into a volute type casing located just above the impeller.

 

Mixed flow, vertical pumps typically are for medium head applications where the specific speed of the pump ranges from 4000 to 9000. At Cooper Nuclear Station, there are several systems which contain vertical, mixed flow pumps. The two systems which contain relatively large vertical pumps of this type are the Service Water System and the Circulating Water System. The Service Water System has four vertical pumps, each rated at 8000 gpm, and the Circulating Water System has four vertical pumps rated at 159,000 gpm each.

 

In a vertical pump, the pump impeller "sits" in a casing or bowl. The outer diameter contours of the impeller vanes match (that is, they are supposed to match) those of the bowl so that the tips of the impeller vanes are always parallel to the surface of the bowl. The parallel gap between the impeller vanes and the bowl, that is, the clearance, significantly influences the efficiency of the pump.

 

If the clearance is too large, water can re-circulate from the high pressure portion

 

downstream of the impeller (above the impeller) to the low pressure portion

 

upstream of the impeller (below the impeller). This not only causes a loss in efficiency of the pump, but it can also lead to accelerated erosion of the bowl.

 

On the other hand, if the clearance is too close, the surface hydraulic boundary layers of the impeller and bowl may interfere with each other. This causes the hydraulic friction due to viscous shear between the two boundary layers to increase, which decreases pump efficiency.

 

Further, if the clearance is much too close, the impeller and bowl may directly interfere and scrape on each other. This causes a significant decrease in pump efficiency. Energy intended for pumping water is diverted and consumed by the impeller grinding itself into the pump bowl. This contact causes permanent damage to both the impeller and bowl and shortens the service life of the pump.

 

Pump impellers and pump bowls are never perfectly round. A pump bowl about 30 inches in diameter may have a diametric tolerance of perhaps +/- 5 mils (1 mil = 0.001 inches). Likewise, the outside diameter of the pump impeller that matches the bowl has a similar tolerance. If the clearance between the pump bowl and impeller is too tight, one or more of the impeller vanes will impinge on a common high point or asperity between the bowl and impeller. When this occurs, the effect is detectable by:

 

a sudden increase in amperage, a decrease in pump output pressure, or both, and

an increase in pump vibrations that have a frequency of the shaft speed times the number of vanes on the impeller contacting the bowl. (Note: when there are two symmetric high spots in the bowl, as would occur if it were elliptical, the frequency might be two times the shaft speed times the number of vanes making contact.)

Between the two extremes of too tight and too loose, there is a "just right" clearance dimension. This "just right" clearance dimension allows the boundary layers of the pump impeller and bowl to slide over each other with minimal shear, but is not so large as to allow excessive re-circulation between the upstream and downstream sides of the impeller. At the "just right" clearance, pump efficiency will be maximum.

 

Impeller clearances are usually specified by the manufacturer. To provide a "feel" for the magnitude of typical impeller clearances, Table 1 is provided.