Abstract
This chapter deals with the calculation methods essentially common to all impellers and diffusing elements regardless of the specific type. The details of calculation and design of the various types of impellers and collectors are discussed in Chap. 7.
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Notes
- 1.
With profiled blades, the effect of the blockage may not be easily defined in certain conditions. Generally, e1 must be selected where the cross section is narrowest relative to the next blade. The effect of the angle λ (if any) must be considered iteratively.
- 2.
Recirculation normally occurs at partload below q* = 0.5–0.7 (Chap. 5). It may, however, occur even near the best efficiency point when extremely wide impellers are used (for example in dredge pumps).
- 3.
When pumping oils or other media of high viscosity, head and efficiency are severely reduced compared with the pumping of water, Chap. 13.1.
- 4.
The sound power radiated as air-, fluid-, and solid-borne noise is negligibly small compared to all other losses.
- 5.
This experimental finding follows from data in [35]; it cannot be deduced by inserting half the angular velocity in the equation given earlier.
- 6.
- 7.
The impeller sidewall gap integration according to Table 9.1 is recommended for more thorough investigations.
- 8.
It is open to debate whether ε/s or ε/2s is more relevant for small clearances. Undoubtedly the hydraulic diameter is dh = 2 s. Considering the structure of the flow one may rather tend intuitively to select ε/s, which could be viewed as a local obstruction to the flow.
- 9.
In order to derive these relationships the measurements in [21] were recalculated into a more general form.
- 10.
The mentioned exponent does not imply a contradiction to Eq. (T3.5.6a) which refers to different pumps with optimally adjusted mechanical equipment, while the scaling of the mechanical losses Pm of a given pump assumes given mechanical components which are over-dimensioned at reduced speed.
- 11.
Exceptions are axial pumps with very high specific speeds, which under certain conditions, have to be designed without diffusing elements, Chap. 7.6.6.
- 12.
The relationship ηh = η0.5 which is sometimes employed does not furnish any useful values either at very low overall efficiencies (small pumps) or at low partload.
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Gülich, J. (2014). Pump Hydraulics and Physical Concepts. In: Centrifugal Pumps. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-40114-5_3
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