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Fluid Mechanics II 2010 (2006 Ad).pdf - DSpace at CUSAT

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BTS (C) — IV — 10 — 015 F<br />

B. Tech Degree IV Semester Examin<strong>at</strong>ion, April <strong>2010</strong><br />

Time : 3 Hours<br />

Cus<strong>at</strong> Digital Library Service http://dspace.cus<strong>at</strong>.ac.in/<br />

CE 405 A/B FLUID MECHANICS H<br />

(<strong>2006</strong> Scheme)<br />

PART - A<br />

(Answer ALL questions)<br />

I. (a) Compare specific energy curve and specific force curve.<br />

St<strong>at</strong>e the conditions under which the rectangular section of an open channel<br />

will be most economical. Derive these conditions.<br />

Distinguish between backw<strong>at</strong>er curve and draw down curves. Give examples<br />

for each.<br />

Sketch the jump position on a stilling basin for various tail w<strong>at</strong>er conditions.<br />

Prove th<strong>at</strong> the maximum efficiency of a jet impinging on a series of moving<br />

fl<strong>at</strong> pl<strong>at</strong>es is 50%.<br />

(t) How can the best performance curve be obtained with the help of characteristic<br />

curves of a reaction turbine?<br />

Discuss few methods adopted to increase the efficiency of centrifugal pumps by<br />

altering the shape of the casing.<br />

Discuss the condition under which neg<strong>at</strong>ive slip occurs in reciproc<strong>at</strong>ing pumps.<br />

PART — B<br />

Maximum Marks : 100<br />

<strong>II</strong>. (a) In a rectangular channel 3.5 m wide laid <strong>at</strong> a slope of 0.0036, uniform flow occurs<br />

<strong>at</strong> a depth of 2 m. Find how high can the hump be raised without causing afflux.<br />

If the upstream depth of flow is to be raised to 2.5 m, wh<strong>at</strong> should be the height<br />

of the hump? Take Manning's n equal to 0.015.<br />

(8 x 5 = 40)<br />

(4 x 15 = 60)<br />

(b) W<strong>at</strong>er flows in a channel of the shape of isosceles triangle of bed width 'a' and<br />

sides making an angle of 45° with the bed. Determine the rel<strong>at</strong>ions between depth<br />

of flow 'd' and bed width 'a' for maximum velocity condition and for maximum<br />

discharge condition. Use Manning's formula and note th<strong>at</strong> 'd' is less than 0.5 a.<br />

OR<br />

(8)<br />

<strong>II</strong>I. (a) A flow of 100 litres per second flows down in rectangular labor<strong>at</strong>ory flume of width<br />

0.6 m and having adjustable bottom slope. If Chezy's C is 56 determine the bottom<br />

slope necessary for uniform flow with a depth of flow 0.3 m. Also fmd the conveyance<br />

and st<strong>at</strong>e of flow (ie. tranquil or rapid).<br />

(7)<br />

(b)<br />

A trapezoidal channel has a bed width 10 m and side slopes of 2 horizontal to 1 vertical.<br />

<strong>at</strong> a section 200 m downstream the bed rises by 0.08 m gradually, bed width increases<br />

to 0.15 m and side slopes become 3 horizontal to 1 vertical. Rise in bed level, increase<br />

in bed width and fl<strong>at</strong>tening of side slopes are gradual. Flow r<strong>at</strong>e in the channel is<br />

200 m3 /s and the flow depth <strong>at</strong> the upstream section is 7 m. If Manning's n = 0.035,<br />

estim<strong>at</strong>e the depth <strong>at</strong> the downstream section.<br />

(8)<br />

(Turn Over)<br />

(7)


IV. (a) St<strong>at</strong>e and discuss the assumptions made in the deriv<strong>at</strong>ion of the dynamic equ<strong>at</strong>ion for<br />

gradually varied flow starting from first principles derive equ<strong>at</strong>ion for the slope of the<br />

co<strong>at</strong>er surface in gradually varied flow with respect to (i) channel bed (ii) horizontal.<br />

(b) Show th<strong>at</strong> the gradually varied flow equ<strong>at</strong>ion for flow in a rectangular channel of variable<br />

width B may be expressed as<br />

Qty dB<br />

dY S - +(j<br />

dx<br />

dx<br />

1<br />

n2 B<br />

gie<br />

(a)<br />

OR<br />

Show th<strong>at</strong> the head loss in a hydraulic jump formed in a rectangular channel<br />

V<strong>II</strong>.<br />

(b)<br />

(vi —V2)3<br />

may be expressed as AE =<br />

2 g(V, - V2).<br />

2<br />

A horizontal rectangular channel 3 m wide and 2 m w<strong>at</strong>er depth conveys w<strong>at</strong>er <strong>at</strong><br />

18 m3/s. If the flow r<strong>at</strong>e is reduced to 2/3 of it's original value, compute the magnitude<br />

and speed of the upstream surge. Assume th<strong>at</strong> the front of the surge is rectangular and<br />

friction in the channel is neglected.<br />

(a) Explain with sketches the working of an oil pressure governor. (7)<br />

(b) Show from the first principles th<strong>at</strong> the peripheral coefficient of a pelton wheel is 0.5. (8)<br />

OR<br />

Show th<strong>at</strong> in a turbine with radial vanes <strong>at</strong> inlet and outlet and oper<strong>at</strong>ing under head 'h',<br />

if the velocity of flow <strong>at</strong> outlet is C times th<strong>at</strong> <strong>at</strong> inlet, the peripheral velocity `u' and the<br />

hydraulic efficiency 'Rh' are given by<br />

2gh 2<br />

u<br />

-<br />

2 + c 2 tan 2 a ' 2 + c 2 tan2 a<br />

where a is guide de blade angle<br />

Assuming th<strong>at</strong> the radial component of flow of fluid through a centrifugal pump<br />

remains constant and th<strong>at</strong> the fluid enters radially, prove th<strong>at</strong> the r<strong>at</strong>io of the pressure<br />

head Hp to the velocity head Hv cre<strong>at</strong>ed by an impeller neglecting the losses is given<br />

by Hp ((<strong>II</strong>—VAcot Pi , where U1 is the speed of impeller <strong>at</strong> outlet, Vf,<br />

Hv U, +Vf, cot 13<br />

is the veloety of flow and /3 is the exit angle of impeller blades. Hence show th<strong>at</strong><br />

, — Vf, cot p)<br />

ideal efficiency of the impeller is given by ri =(U.<br />

2U,<br />

OR<br />

Working from the first principles show th<strong>at</strong>, in a single acting reciproc<strong>at</strong>ing pump<br />

the work done against pipe friction, if large air vessels are fitted near to the cylinder<br />

on both suction and delivery pipes, compared with th<strong>at</strong> done if there are no air vessels<br />

is (%2 g2).<br />

***<br />

(15)<br />

(15)<br />

(15)

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