Wednesday, 24 October 2012

A Note on Pump Selection (1)


Selecting Centrifugal or Reciprocating?

Although centrifugal pumps are the first option in a pump selection process because of lower cost, simplicity, reliability and smooth flow characteristics, there are some occasions when positive displacement pumps (reciprocating or rotary) might be more desirable. These occasions can be classified as follows:
  1. Very high head, especially when combined with a low capacity; 
  2. Low speed drivers;
  3. High efficiency requirements over a range of pressures;
  4. Constant capacity requirements over a wide range of heads;
  5. Variation of head requirements over a wide range;
  6. High viscosity;
  7. Emulsification;
  8. Accurate control of flow requirement in low flow applications.
There are some notes that should be considered together with the above-mentioned selection criteria:
  • There is a specially designed type of centrifugal pumps for low-flow, high-head applications. This is high speed integrally geared vertical inline pump which is identified by API classification OH6 and is known as “Sundyne” in industry. As a guideline, reciprocating pumps are selected for low-flow, high-head applications when service conditions are outside the hydraulic coverage range of Sundyne pumps as presented in below Figure. Of course NPSH and minimum flow requirements should be carefully investigated when selecting a Sundyne pump.
  • Although initial costs of small reciprocating pumps are competitive with centrifugal pumps, for capacities over 200 gpm they are usually more expensive.
  • When service requirements permit using either a centrifugal or a reciprocating pump, the operation and maintenance cost should be carefully considered. Maintenance costs of reciprocating pumps are usually higher because of moving parts, valves and sliding contacts.
  • For viscosities above 500 SSU and below 8000 SSU usually reciprocating pumps are considered. For viscosities above 8000 SSU rotary pumps are the better options.
 Sundyne pumps hydraulic coverage

Tuesday, 9 October 2012

NPSHR Variations with Changing Speed or Diameter


When dealing with NPSHR, the best practice to determine the variations is to develop a NPSH test. However there are some other methods to predict the trend or approximately calculate the NPSHR in new conditions.

1. Speed Change

According to API 610, only 3% variation in speed is allowed for centrifugal pumps performance test; “Unless otherwise agreed, the test speed shall be within 3% of the rated speed shown on the pump data sheet. Test results shall be converted to anticipated results at the rated speed.” For this conversion ASME PTC 8.2 (Performance Test Code for Centrifugal Pumps) suggests the following formula based on affinity laws



According to HI standard, “if a pump operates at or near its cavitation limit, the limiting NPSHR value may vary other than as the square of the speed”. Another exponent (other than 2) can be suggested by pump manufacturer for the specific pump at hand. Also some pump engineers believe that exponent 2 is accurate enough when the speed is increased but for the speed reduction an exponent equal to 1.7 will give better approximations.

2. Diameter Change

In this case the affinity laws won’t be applicable to predict NPSHR value and the only way to obtain the accurate NPSHR is testing. But yet there are experimentally acquired trends that help in prediction of NPSHR value.

Some experimental studies have shown that for low specific speed pumps the variation of NPSHR is negligible when the impeller diameter is trimmed. It has been shown that when the pump specific speed is low, trimming the impeller diameter even to 70% of full diameter won’t change NPSHR.

As the specific speed increases, NPSHR will be affected by variation of impeller outer diameter. The following figure show that NPSHR will increase for a trimmed impeller diameter and the value of this increase become greater for high specific speed pumps. So it can be concluded that the impeller diameter of mixed flow and axial flow pumps has a strong influence on pump NPSHR.


NPSHR variation with impeller outer diameter and specific speed [Source: Kondo, Yamada, “Dose Impeller Affect NPSHR,” International Pump Users Symposium 1985, pp. 29-35]