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