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Fluid Mechanics and Thermodynamics of Turbomachinery, 5e

Fluid Mechanics and Thermodynamics of Turbomachinery, 5e

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Basic <strong>Thermodynamics</strong>, <strong>Fluid</strong> <strong>Mechanics</strong>: Definitions <strong>of</strong> Efficiency 53<br />

where c2 — is the mean square <strong>of</strong> the velocity in the cross-section <strong>and</strong> Q = AU, i.e.<br />

From eqn. (2.56) the change in static pressure is found as<br />

(2.57)<br />

(2.58)<br />

From eqn. (2.51), with eqns. (2.47a) <strong>and</strong> (2.47b), the diffuser efficiency (or diffuser<br />

effectiveness) can now be written:<br />

Substituting eqn. (2.58) into the above expression,<br />

where v is the total pressure loss coefficient for the whole diffuser, i.e.<br />

(2.59)<br />

(2.60)<br />

Equation (2.59) is particularly useful as it enables the separate effects due the changes<br />

in the velocity pr<strong>of</strong>ile <strong>and</strong> total pressure losses on the diffuser effectiveness to be found.<br />

The first term in the equation gives the reduction in hD caused by insufficient flow diffusion.<br />

The second term gives the reduction in hD produced by viscous effects <strong>and</strong> represents<br />

inefficient flow diffusion. An assessment <strong>of</strong> the relative proportion <strong>of</strong> these<br />

effects on the effectiveness requires the accurate measurement <strong>of</strong> both the inlet <strong>and</strong> exit<br />

velocity pr<strong>of</strong>iles as well as the static pressure rise. Such complete data is seldom derived<br />

by experiments. However, Sovran <strong>and</strong> Klomp (1967) made the observation that there<br />

is a widely held belief that fluid mechanical losses are the primary cause <strong>of</strong> poor performance<br />

in diffusers. One <strong>of</strong> the important conclusions they drew from their work was<br />

that the thickening <strong>of</strong> the inlet boundary layer is primarily responsible for the reduction<br />

in hD. Thus, insufficient flow diffusion rather than inefficient flow diffusion is <strong>of</strong>ten<br />

the cause <strong>of</strong> poor performance.<br />

Some <strong>of</strong> the most comprehensive tests made <strong>of</strong> diffuser performance were those <strong>of</strong><br />

Stevens <strong>and</strong> Williams (1980) who included traverses <strong>of</strong> the flow at inlet <strong>and</strong> at exit as<br />

well as careful measurements <strong>of</strong> the static pressure increase <strong>and</strong> total pressure loss in<br />

low speed tests on annular diffusers. In the following worked example, to illustrate the<br />

preceding theoretical analysis, data from this source has been used.<br />

EXAMPLE 2.5. An annular diffuser with an area ratio, AR = 2.0 is tested at low speed<br />

<strong>and</strong> the results obtained give the following data:

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