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FLUID MECHANICS (II)
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1-
Assignment 7
Calculate the maximum acceleration allowed. Then if the acceleration is increased
by 2A% (a=1.2a.",,). Calculate the intensity of pressure at A & B and the volume
spilled. (width = 4m)
2- A steady flow of air. The properties are given below
Work is done by a compressor on the system at the rate of 1000kW. Find P3 and Q
(state its type)
(For air R=287 J/kgK, Cp=1005 J/keK)
Section A (m') Q (m'ls) P {bar) Z (rn) T ("C)
1 inlet 0.3 2 1.5 1- 20
2 outlet o.7 0.8 2 2 30
3 outlet o.2 1 ? 1.5 50
3- Air o ws steadily as shown in g ure through a compressor that adds 5kW to thefluid. Estimate Vr, Q and state its type
dr=15cm
Pr=3bar
Vr=?
tr=5OoC
dz=10cm
Pz=5bar
V2$rn/s
tz=70"C
4- For the pump shown sketch TEL and
P',=? . Also calculate the manometer
momentum delivery head.
HGL then determine the pump output power
(H,,) manometer suction head, (H,o)
Lz=20m
dr=5cm
F=0.02
Delivery pipe
Z=2m
Lr=5m
dr=15cm
F=0,02
Suction pipe
5- Given for a centrifugal pump the following r1=0.1fft, rz=0.18m, br=bz-0.05m,
fit : 3A", Fz = 20", n=1440rPm'
Estimate:
a- The design diameter
b- The water power
c- The head t
6- The following is the performance of a pump at n-1140 rpm
Q (m'ls) 0 0.05 0.1- 0.1-5 4.2 o.25 0.3H (m) 10s 104 LO2 100 95 85 67P,(kW) 100 175 135 171 242 228 249EfficiencvHrr, (m)
(pwater - 99\kg /m3)]f the pump operate a system whose stac head (lift) =50cm through a pipe of?200m, d=0.Lm and F=0.03
Determine:
a- The design Q & H at (BEP) best efficiency pointb- The pump specific speed
c- The pump operating point (Q and H at this point)
What should be the design Q, P and H if the pump speed is doubled?
A pump draws water from a reservoir whose surface pressure is 90kPa (abs) if thehead loss frorn the reservoir to pump is 2m. where should the pump be placed
above the suction levelto avoid cavitationlf (NPSH) required 4m and P"p=4kPa (abs)
7-
#,LW
Ain Shams University
Faculty of Engineering
New Program
ENGR 350 Fluid Mechanics IIExoerimenta
Ais;y, J I
Presented to:
Presented by:
Prof. El-samanoudy
Ahmed Hassan Ibrahim
P.MANF
Assignment 7
1- Calculate the maximum acceleration allowed. Then if the acceleration is increased
by 20% (a=1.2a,.,). Calculate the intensity of pressure at A & B and the volume
spilled. (width = 4m)
4
')') t\\i,I - ,{ ax in,r ur,n crc"*lar rr.ii*-r 1 r', "r ,eLA'I V
Qx
{ons: _ e_ses_?oAi-,n?o * S.tt
f)/Hr.i 0,381 r,riSz
P_* ?LL 2_
f-I P\CJ,
YZ.
a\qz
C(::
:elo*S
t,2_A- Ctrl
1,2 ( L.3Lr
^tu71 LQ -- t,
= -l ,c57z6flZ,,,s: ?o/?1-6 3{ 1 iln LO
Z_
'n /s,z ?,tg_q4: 7 '61ts 3
n{iel4,h/-._'
]I
1.\
D14 =
\r'
16'Ln
ilz* ? 1
,:1,'r6t";ls''*t- = t e 7 :
= Yf q?-l-%)lno\ 'a
\).E =\'he x( *ry-k )tu ; (+ - z e,
2 e. mb? kFq
\Lp i rkd-\/. , *(/r t'r{ {: 4 [+*:
L
)9X\*c\
-r\s"
-) f* -l
,)
Section R (m') Q (m'ls) P (bar) z (m) T ("C)
f. inlet 0.3 2 1.5 t 202 outlet 0.7 0.8 2 2 303 outlet 0.2 1 ? 1.5 50
2- A steady flow of air. The properties are given below
Work is done by a compressor on the system at the rate of 1000kW. Find P3 and Q(state its type)
(For air R=287 J/kgK, Cp=1005 J/kgK)
1 764 k.7 /*:n .')l't5 \i)*'
vl
tlv?
v3
I
q:= I+ *>3 x I --> \ -"/ -s,
+
\ .7 zi, t r/^.AU
-_-___:__€l:\6C,tBTkPa
--\ .
ltI t'ta! fr'na - \h r
:
I
I
zG+
2,3x ",0 (
,
\,12rx , (,7i4(.(
oIr/^ .is (t, U2' \" : -z-
\3 i, r y ;/
/,,t,
;,jl Yl ,/.\, .'.rlX iJ
I
Q+\xrD6:+
' ','l-Yt ,1\J v , ,r"I A t')"7r,;$l.Jil{'i
/ F.
!I /,_\J L_i
Co.rl t4-). r
A1l
, ,.1 ..':j
rti
. l. \lV
Air flows steadily as shown in figure through a compressor that adds 5kW to thefluid. Estimate Vr, Q and state its type
dz= 10c m
dr=15cm
Pr=3bar
Vr=?
tr=50oC
Pz=Sha r
Vz=S mls
tz=70oC
-:*b
fn: nnt =\, l-r 1 .a
I -+l-- ) r.ll,:: 1-U*-**- X tt / 1{\2L ( -j X (2-l- -;,,) -1- \t" -) tV'
rnzJi-\\^,[-!ff,,\ArV,\ r'T',/\ -.-5irut ,I_l-,_rf c r,* I t l-4r f.;,7;; "r \ ,) . i
= 3.+x?,*, lSvr
fY= (J,t
=.
tq4 k,, l.t:
;Vh,.l\
" rt:,of (L
a}-)w,i\- lr) +
lr
* \,V. \l--1,
t-l\-ll )L. X
,:,'\ ttiti *\4Ll-\
(.*]'- ro) +
**V:4 ,r'\lI " (,' -/r]
,-l \)lz1
(ro,rr: { i 1?-. ,) 4";'l 'l]triJC Cr ,-r:1 r'*"l. -71 t A/
C
ICoo lr,"*,()
(rrit *),. q r,i(l
t, r*-)
4- For the pump shown sketch TEL and HGL then determine the pump output power
P*=? . Also calculate the manometer (Hrr) manometer suction head, (Hra)
momentum delivery headl.
Lr=20m
dr=5cm
F=0.02
Delivery pipe
Lr=5m
dr=15cm)
Suction pipe
\ivl :
V. -,
Il.1l
F=0.021 ,) 1 , ) , .\ I.*:--...,-. : ,..-.... :i :: O,l-(* ml5
;: / t- |rr 1tt-l
rl - tll**-[, h,,lr-l3- L+ \'; :
1 ._-f,/\
rr L iI 5 + /ltt "r,i, o*i:r- r\ C)\'-tu JI+1.,:.'-7,_,"
(, ; -":
7'" !
!-- ; , t l' ,1^
l\tlrnl( -=:
t\,.1
r (r=, )'
: lL,\tp
, ' .; Lj i ln,./ t.
a , i t 1.li-.1-- '\ i; "
-) , --r
L,U
hi, ,
!* iu;" .:, j,('
;:.)
t:.':)
\t *;i-t /rlM:L-
r"
:t'
'.i
I i_)-:,.,.1.t-)rtr-., )
\'ht'!l
+ o.o(2.ot ,^
c t k? $'{i?
i" v\l
svcttigr-v{ I
Q=10 lit/
5- Given for a centrifugal pump the following r1=0.1lrr, rz=0.18m, br=bz-0.05m,
fit : 30", fi, : 20", n=1440rpm.
Estimate:t\
a- The design ffi J,'- :'[ .'i, r'x'
b- The water power \
c- The head
(./J : LTt n*--*a-#bo
Lc, P,
LonSc\l''t t
I
v^\
6.? 0
V, - -.- u'rr*-mr- - Lorfr
Vn,'
/.N.. ,/ \,1,Y un'\
'/' 'i -* --f*.,h-\
.tl,I -\u,I -\/!\-
I ---I ---l-Ail uP\X1 : grt' i,l1 "' UJ r{q
6.J *lrrlvnr
\1,u*\-v
?rf rr b,\
= --. tV
--.-.-3 fl { e'tr x *"
a ,27 35 {r.'I
_ t\)ZlT { 2 tO, ' zTxo,r6xo-,b z 4'637tl
U}
rJ
vn, =
- r I ''t t tql leErvn :-l)vlCr\r:^,, V1 = /=:+:t, X--t-l'(j
\ 3,xbz n I *r \1, *
\r . .). ;' '1 v r.l.) ( l3 tS)
:-;) \ / t Uf r ) I I.tvl t
\:'v(
1*],; xn,2735x
t"tte1 -) ):, fi^)\-)u'*-rL
l^f1 t>te L, (,
Ji
llIt .'rt \/,,i-l J2\",..i_'l
{
nl)I ttt( r:,*,-,I :\ E
kw
6- The following is the performance of a pump at n-1140 rpm
(pwater - 99\kg /m3)lf the pump operate a system whose static head (lift) =50im through a pipe of
l?-00m, d=O.tm and F=0.03
Determine:
a- The design Q & H at (BEP) best efficiency point
b- The pump specific speed
c- The pump operating point (Q and H at this point)
What should be the design Q, P and H if the pump speed is doubled?
B f l I C l('/1r J, :d
t3--J-cl_*p-
J
1
XOHP" x r,>'
r l.i r'* ,,., . x lo-( = <:.7 L: = 2
" I
nl-t
OA
I)Ycrrn
* zo2 k$/
N= cr{
\\
I
:rr"/,ti"'"
13 4
Q (m'ls) 0 0.05 0.1 0.15 0.2 o.25 0.3H (m) 105 r04 L02 100 95 85 67
P,(kW) 100 175 135 171 202 228 249Efficiency, 0 fiALJ ?3 7\ 12
a, l:r\ 7rHrr, (m) :-a c-/ /.8 ,b /.. l__1:) IL 141 \c;
\\1 [5,;1=,
tl
U
1-l *cL i qItl--'l ., I .,^\
,
\l+,ri ;.
r tlvi*^^lL \...t' :'I) rr'\
/,,
trrL u 1z+ *-I;-l: --l" -lJ'*
U\r*- l( :)
t
)l+or i.K:
r .,rf,U nr
-KtrL_ _x ( c oix j-) i) Itr A i 'l -.lr(''1./)lv-ta1r x Q?r >'lJ' vln4')
,/t/Optr,3\i,'.,, "r:ndt\i*,,r
a = C,\t3 ,vl3l sr-t =
g2 5 rn,l--
Tfr -i at,v t- , I(r;N I\ / ,-,_/ / |
Q.
N, :N, =
o.4
/\l
ZN:lrn'l s
J[z =
/i\-*
l',I ...
i-i
r ',\_/l
i! | -.,
I(l'l/1
t
\-,rlt\
rit-,-.. . .i1
,"\'1 ' )-o))\- :^ -li,/t/\..)\ b LW
-o-
€----
L-\
t"t---o-
fr--No
1-c--
'a
,*, -, -+-._+_-_ ..___--_-.-; q .9
-s-- - -r4- --''- r^ --t'-? _9---- --'-F------*)- -
-T9'-,o
1- A pump draws water from a reservoir whose surface
head loss from the reservoir to pump is 2m. where
above the suction level to avoid cavitation
lf (NPSH) required 4m and P,p=4kPa (abs)
pressure is 90kPa (abs) if the
should the pump be placed
1lI; 1t -
") ..,
t'
v
Ru - ba l ,rvf< r,
L,,L-!'--x ,. ''/,
l rA - ll 4
s oll I -->nL Lt,r+.-.
---\;-*-Nt
4\,-,\ '.
(
gr; Xr) -
') r-i * ';.---
--v'/L--- ,
I *-
{/ i
/l !'. : .-l
'L l6(1