Parameters Fan

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Parameters Fan

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On page Parameters you have to put in or to modify parameters resulting from approximation functions in dependence on specific speed nq or flow rate Q. See Approximation functions.

For details of how to handle the parameter edit fields please see Edit fields with empirical functions.

 

Parameter and efficiency values can be handled manually or can be switched to automatic update by the checkbox on top of the page. Then the default values are used always, even after design point modifications (see Global setup).

If the automatic mode is not selected the current default values can be specified by one of the following options:

globally by the button on top of the page

regionally by the default button within the Parameters or Efficiency region

individually by the default button within the input field when selected

Parameters

The panel Parameters allows defining alternative parameters in each case for the calculation of the following impeller diameters:

inlet

outlet

dS1, dH1

dS2, dH2

For dS2-calculation

Work coefficient ψ

(= pressure and head coefficient)

dimensionless expression for the specific energy:

0.7  ...1.3 centrifugal impeller

0.25...0.7 mixed-flow impeller

0.1  ...0.6 axial impeller

high small dS2, flat characteristic curve
low high dS2, steep characteristic curve

Diameter coefficient δ

according to Cordier diagram (see Dimensions)

Flow coefficient φ

dimensionless flow rate

high small dS2, flat characteristic curve
low high dS2, steep characteristic curve

 

For dH2 calculation

Diameter ratio dH2/dS2

Can be estimated under assumption β2 = 90° @ hub and cu·u = const. by:

 

For dS1/dH1-calculation

Meridional velocity ratio cm2/cm1

Diameter ratio dH1/dS1

strictly axialdH2 = dH1 and dS2 = dS1
const. hubdH2 = dH1
const. middM2 = dM1
const. shroud dS2 = dS1

Efficiency

In panel Efficiency you have to specify several efficiencies. You have to distinguish between design relevant efficiencies and efficiencies used for information only:

Design relevant

total-total efficiency ηtt

volumetric efficiency ηv

additional total-total efficiency ηtt+ (displayed for information only, see Global setup)

Information only

mechanical efficiency ηm

motor efficiency ηmot

The additional total-total efficiency ηtt+ is used for impeller dimensioning in order to compensate additionall flow losses .

The losses resulting in energy dissipation from the fluid form the internal efficiency.

Impeller and mechanical efficiency form the overall efficiency (coupling efficiency) of the stage ηSt.

When considering motor losses additionally the overall efficiency of the stage incl. motor ηSt* is defined.

PQ: power output, see above

PD: mechanical power demand (coupling/ driving power)

Pel: electrical power demand of motor

 

The following summary illustrates the single efficiencies and their classification:

classification

efficiencies

Relevant for impeller design

stage

impeller

ηtt+

additional total-total

yes: for energy transmission

ηtt

total-total

ηV

volumetric

yes: for flow rate

 

ηm

mechanical

no: for overall information only

stage incl. motor

electrical

ηmot

motor

The obtainable overall efficiency correlates to specific speed and to the size and the type of the impeller as well as to special design features like bypass installations and auxiliary aggregates. Efficiencies calculated by approximation functions are representing the theoretical reachable values and they should be corrected by the user if more information about the impeller or the whole pump are available.

The hydraulic efficiency (or blade efficiency) describe the energy losses within the pump caused by friction and vorticity. Friction losses mainly originate from shear stresses in boundary layers. Vorticity losses are caused by turbulence and on the other hand by changes of flow cross section and flow direction which may lead to secondary flow, flow separation, wake behind blades etc.

The volumetric efficiency is a quantity for the deviation of effective flow rate Q from total flow rate inside the impeller :

(rising with decreasing tip clearance)

The mechanical efficiency mainly includes the friction losses in bearings and seals:

(rising with impeller size)

Total-total and volumetric efficiency are most important for the impeller dimensioning because of their influence to and/or . The mechanical efficiency is affecting only the required driving power of the machine.

 

If the check box "Use η for main dimensions (otherwise for βB2 only)" is set, then main dimension calculation is done on the basis of Yeff= 0.5(Y/η+Y). Otherwise Y - specific work without losses - is used.

Information

In the right area of the register Parameter you can find again some calculated values for information:

Required driving power

Power loss

Internal efficiency

Stage efficiency

Stage efficiency incl. motor

Assembly

Pressure difference

Remark

inline installation,

resistance coefficients according to Wallis

inline installation, Carnot type diffuser

resistance coefficients according to Wallis

inline installation, swirl assumed to dissipate in duct → pseudo total-to-total pressure rise

resistance coefficients according to Wallis

exhaust installation

potential pressure recovery in exhaust jet not taken into account