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Final Semi 20182019 03 04.pdt - Adobe Acrobat Reader DC File Edit View Window Help Home Tools ilovepdf merged (4). Final Sem

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Answer #1

Solutions

Given Data :-

T1 = 90 mm

r2 = 150 mm

bi 10 mm

b2 = 7 mm

0 B1 = 25

s = 45°

N = 1200 rpm

C - 90*

t1 0

.

Velocity Diagram at inlet :

Vrel,1 V1 = Vr1 B1 αι U

.

Velocity Diagram at outlet :

Vrel.2 V2 Vr2 \B2 d2 Viz U2

.

The actual inlet flow area

:. A1 = (21 – 0.12(21))rıbı = 1.76arib

:. A1 = 1.767(0.09) (0.01)

1. A1 = 4.9763 x 10-3 m

.

The actual outlet flow area

A2 = 1.767122

:. A1 = 1.767(0.15)(0.007

:. 42 = 5.805664 x 10-3 m? 2

.

The speed of the blade at inlet and exit:

.:. Uι 2πη,Ν 60 2π(0.09) (1200) 60 Ξ 11.3098 m/s

::U2 = 21r2N 60 27 (0.15) (1200) 60 = 18.85 m/s

.

The velocity in the radial direction at inlet is written as:

V1 = V, = Uitan 31

.: V1 = (11.3098)tan 25

:: V1 = 5.27385 m/s

.

Part i)

The discharge of the pump is written as:

::Q = A1V1

::Q = (4.9763 x 10-) (5.27385)

3 ::Q = 0.026244 m S

.

From discharge we get, the radial component of velocity at outlet;

:: V-2 2

.:: Vr2 = 0.026244 5.805664 x 10-3

:: Vr2 = 4.52042 m/s

.

Part ii)

\textup{From the velocity triangle at outlet we get; }

\therefore V_{t2}=U_2-V_{r2}\cot\beta _2

.: V2 = 18.85 18.85 – 4.52042 cot 45

\therefore V_{t2}=14.3296\, \, m/s

.

Vr2 As we know, tan 02 = V12

\therefore \tan\alpha _2=\frac{4.52042}{14.3296}

..0 = 17.51°

.

Part iii)

\textup{The theoretical pump head is given as:}

\therefore H_{th}=\frac{U_2V_{t2}-U_1V_{t1}}{g}=\frac{U_2V_{t2}}{g}

:: Hth = (18.85) (14.3296) 9.81

Нth 27.5345 m

.

\textbf{Part iv)}

\textup{The brake power of pump is given as:}

\therefore \dot{W}_{pump}=\rho g Q H_{th}

:. И, (1000)(9.81) (0.026244)(27.5345 ритр

. W pump = 7088.845 W = 7.09 kW = 9.5063 hp

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