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Gas/Steam Medium 1
17

Gas/Steam Medium

Feb 22, 2016

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Gas/Steam Medium. If the medium is already a gas/steam, the phenomenon that the flow medium will change from the liquid to the gas phase does to occur, thus no cavitation has to be considered . - PowerPoint PPT Presentation
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Page 1: Gas/Steam Medium

1

Gas/Steam Medium

Page 2: Gas/Steam Medium

• If the medium is already a gas/steam, the phenomenon that the flow medium will change from the liquid to the gas phase does to occur, thus no cavitation has to be considered.

• For lower temperature, the sonic velocity is low. In order to avoid supersonic and sonic flows the flow velocity has to lower. But the flow velocity may be desired to be higher.

• Above sonic velocity(supersonic flow) there is an occurrence of shock waves which represent losses.

2

Page 3: Gas/Steam Medium

3

• The nearness of the flow velocity to the sonic velocity a may be expressed using the Mach Number.

• IN general, flow conditions where M=1 and normally also those with M>1 (supersonic flow) have to be avoided.

• The sonic velocity of a gas is:

• Since for a given gas k and R are constant, the locally prevailing temperature determines the sonic velocity a, the danger or reaching sonic velocity is greatest where the temperature is the lowest.

• In general, this is at the suction end of the turbomachine.

aCM

kRTPka

Page 4: Gas/Steam Medium

4

Compressors• The sonic velocity is lowest at the suction end of the impeller,

in the case of multi-stage compressors, at the suction end of the first impeller as here the temperature is lowest.

• The criteria to limit the locally highest velocity below the sonic velocity may be expressed as follows:

• Similarly to avoiding cavitation, an optimum angle βoa can be determined:

8.07.0 toaWM oa The lower value refers to impeller with thick vanes

The higher value to those with thin vanes

22max 1 oaWW

Where Wmax = locally highest velocity in the vane channel near suction end

Experimental value: λ ≈ 0.2 to 0.3

Page 5: Gas/Steam Medium

5

Assuming no pre-rotation (δr=1) and the value of λ the optimum angle βoa is:

The optimum angle which avoids sonic velocity best has value of nearly twice of optimum angle avoiding cavitation best

By applying the above criterion the velocity in the channel near the suction edge is kept lowest. As the velocity decreases the frictional loss also decreases which results a higher hydraulic efficiency.

'3032'1032 00 tooptoa

Page 6: Gas/Steam Medium

6

The Suction Diameter-The Inlet Number ε and the Discharge

Number ε2

Page 7: Gas/Steam Medium

7

• The suction diameter has to be chosen so that βoa obtains its desired value with regard to avoiding cavitation or sonic velocity or with regard to obtaining lowest friction loss at the vane suction edge.

• The following optimum values of βoa were mentioned in the previous chapters:

1

::

;35

:20

:17

0

0

0

roptoa

optoa

optoa

if

vanesrotorofedgesuctionatlossfrictionlowestobtainingneturbomachiallvelocitysonicavoidingCompressor

woasmallest

cavitationavoidingturbine

cavitationavoidingpump

Page 8: Gas/Steam Medium

8

• The suction diameter D1a and the angle βoa are interrelated to each other by the velocity Coma as follows

• A relation between Com and D1a can be found from the velocity triangle at point o:

aoo

om DfAwhereAVC 1

' Cross sectional area at point o

Perpendicular to Com

2

1

1

s

n

r

Ddk

ar

om

ouaa

omoa U

CCU

C

11

tan

Page 9: Gas/Steam Medium

9

It follows

and

alityproportion of factors f,f where

tan2

tan

21

2111

1 Sasoaa

roaaroma DfDwithCfDUC

2

111

4

''

SS

Soma

Dk

VfAVfCfC

3

2

123

2

1

tan'4

tan'8

roaoarS f

fnkV

fkVfD

oaS

roaaromaDfUC tan2

tan 21

oaS

r

S

DfDk

Vf tan2

4

'2

2

1

Page 10: Gas/Steam Medium

10

• The suction diameter Ds may also be determined using the following dimensionless numbers:

• Knowing the value of ε, ε2 , the suction diameter Ds follows from

• The values of ε and ε2 are functions of the shape Number Nshape as can be noted from the following derivation:

Pumps and compressors

Inlet NumberY

omom

CC

YC

2

turbines Discharge Number2

222

2 Y

omom

CC

YC

2

111

SSoom DAAC

Page 11: Gas/Steam Medium

11

VfViffnk

Vffnf

nDfDfC

oaroar

oaSroaS

roma

33

22

312

22

'tan

4tan

tantan2

and omaomoarom CCif

YkVnfff

YC

32/3

223

221

2 tan42

12

where 22/3

2

shapeNYVn

3/23

32

21 tan2

4

shapeoar Nk

fff

3/2

33

221 tan64.1

shapeoar Nk

fff

Page 12: Gas/Steam Medium

12

• The Inlet number for pumps and compressors, assuming δr=1 and k = 1-(dn/Ds)2≈0.8 and the common range βoa =14 to 380 is

3/4

3/2221

2 tan70.2

shapeoar Nk

fff

inletrotoratlossfrictionlowvelocitySonicCavitation

fffwhereNfffto shape

/

1.150.170.0 33

221

3/233

221

As far as the slow-running rotor with Nshape < 0.1 and k =1 is concerned the value of ε may be taken independent of Nshape as

inletrotoratlossfrictionlowvelocitySonicCavitation

to

/

5.01.0

Page 13: Gas/Steam Medium

13

• The values δr and k of water turbines of normal designs areδr≈1 Francis, Kaplan TurbineK ≈ 0.8, Kaplan Turbine, k ≈1 Francis Turbine

• The following table shows some values of ε2 taken from actual designs.

Francis Turbines Kaplan T Dim.

Nshape 0.063 0.065 0.123 0.210 0.34 0.52 0.70 1

ns 70 94 141 237 387 592 797 (metric)

nq 21 28 41 70 114 174 234 (metric)

ε2 0.032 0.032 0.048 0.096 0.152 0.331 0.486 1

βoa 30 23.5 21.3 21.3 18.6 19.4 19.2 degree

Page 14: Gas/Steam Medium

14

• Faster running turbines have higher values of ε2. In case of the Kaplan Turbines ε2 may account up to 0.5.

• This means that the kinetic energy Co2 /2 with which the water is

discharged from the rotor is equal to 50 % of the available energy Y.

• All this kinetic energy would be lost if no draft tube were provided. A draft tube, however, will ‘recover’ part of this kinetic energy.

• As ε2 of fast running turbines is large, these turbines have to be designed with very effective draft tubes. For this reason Kaplan turbines are mostly designed with elbow type draft tubes.

Page 15: Gas/Steam Medium

15

Number of Vanes

Page 16: Gas/Steam Medium

16

• If the number of vanes is small, each vane is loaded much and, hence the pressure difference between both sides of the vane is high.

• This leads to non uniform velocity distribution in the vane channel and very high local velocities may occur. Thus also cavitation or sonic velocity is more likely to occur.

• If the number of vanes is high the vane channel becomes narrow and consequently the friction loss is high.

• Thick vanes do not allow to install many vanes. Generally the thickness of the vanes should be as small as possible observing, however the strength of the vane material, the vibration of the vane and proper profiling if desired.

Page 17: Gas/Steam Medium

17

• Number of vanes

• Pumps and water turbines have mostly cast vanes, radial-flow blowers have sheet metal vanes.

• Axial- Flow

• The above formulas are also applicable to determine the number of vanes of guide vanes.

2sin2 21

erkZ m

where e = length of the mean stream line in meridian section measured between vane in-and outlet

rm = radius of the middle of the line e k = empirical factor = 5 to 6.5 cast vanes = 6.5 to 8(to 12) sheet metal vanes

2

sin,21 21

12

212112

rrrrkZthusrrrandrre m