In the February 2010 issue of Pumps & Systems, I wrote an article on my Excel-based Suction Specific Speed and Suction Energy calculators and how they can be used to predict the onset of suction recirculation. During the past year, I have received several requests to revisit this topic and its application to wastewater pumps.
Clear Water Impellers
Clear water impellers are usually designed for high efficiency, but they can also be designed for low NPSHR. Increasing the eye diameter decreases the inlet velocity and, therefore, reduces the NPSH required to maintain uniform flow. It is this reduction in inlet velocity that causes the NPSHR to drop as flow moves to the left of a typical H/Q curve and when the rotational speed of the same pump is reduced.
These impeller designs can work well as long as flow remains at or near the best efficiency point (BEP). If flow moves too far to the left of BEP, the increased peripheral velocity of the larger eye distorts the flow into the inlet and directs a portion of the flow back out of the impeller (suction recirculation). During recirculation, intense vortices arise and cause low pressure areas that will lead to cavitation and severe pressure pulsations. The effect of the impeller eye diameter on potential suction recirculation can be evaluated using suction specific speed (S or Nss).
Suction Specific Speed
Igor Karassik and two of his associates, G.F. Wislicenus and R.M. Watson, developed suction specific speed (S) in 1937 during their tenure at Worthington Pump. It is a dimensionless number that describes the suction conditions that occur due to the relationship of rotational speed, flow and NPSHR. Its development overcame the limitations of the Thoma-Moody constant, which attempted to describe suction conditions by relating head to NPSHR.
S can range from about 5,000 to over 20,000 and is computed by the equation
N is the rotational speed
Q is BEP flow
Several pump organizations including the Hydraulic Institute (HI) and American Petroleum Institute (API) recommend an S of under 10,000 to maintain a reasonable range of flows without the potential for suction recirculation.
Wastewater pump impellers are not intentionally designed for low NPSHR, but the relatively large eye required to pass solids can often lower their NPSHR and increase the value of S. The H/Q curves for some higher flow wastewater pumps show a continuous increase in NPSHR as flow moves to the left of BEP. This is exactly the opposite of the NPSHR versus flow for clear water pumps with normal eye diameters. In the case of wastewater pumps, discharge recirculation at the vane exits can also increase the possibility of suction recirculation. This is due to the lack of any vane overlap on most wastewater impellers, which results in the onset of discharge recirculation at higher flows than expected. For more information on suction and discharge recirculation, see Igor Karassik's three part series “Centrifugal Pump Operation at Off-Design Conditions. It is available on the “Other Pump Topics” page of www.PumpEd101.com.
Figure 1 shows the S calculation for an 8-inch, 1,780-rpm wastewater pump with a BEP flow and head of 3,000 gallons per minute at 135 feet and a specific speed (Ns) of 2,450. BEP efficiency and NPSHR are 82 percent and 10 feet. The calculated value for S is 17,337.
Figure 1. Suction specific speed calculation for a wastewater pump
Figure 2 shows the minimum continuous stable flow (MCSF) for pumps with a given Ns and S. MCSF is the flow at which the onset of suction recirculation can begin. The Y axis is S and the X axis is percent of BEP flow. The three curves represent various pump Ns. Note that MCSF is dependent upon both Ns and S.
Figure 2. Minimum continuous stable flow