1.10 Water passes through a pipe of diameter di=0.004 m with the average velocity 0.4 m/s, as shown in Figure.
1) What is the pressure drop ¨C?P when water flows through the pipe length L=2 m, in m H2O column?
2) Find the maximum velocity and point r at which
L it occurs.
3) Find the point r at which the average velocity equals the local velocity.
r 4£©if kerosene flows through this pipe£¬how do the variables above change£¿
£¨the viscosity and density of Water are 0.001 Pas and 1000 kg/m3£¬respectively£»and the viscosity
Figure for problem 1.10 and density of kerosene are 0.003 Pas and 800
kg/m3£¬respectively£©
solution: 1£©Re?ud???0.4?0.004?1000?1600
0.001from Hagen-Poiseuille equation
?P?h?32uL?32?0.4?2?0.001??1600 d20.0042?p1600??0.163m ?g1000?9.812£©maximum velocity occurs at the center of pipe, from equation 1.4-19
so umax=0.4¡Á2=0.8m
3£©when u=V=0.4m/s Eq. 1.4-17
V?0.5umaxuumax?r?1???r?w2??? ?2V?r?1???0.5 ?£½0.004u??maxr?0.0040.5?0.004?0.71?0.00284m
4) kerosene:
Re?ud???0.4?0.004?800?427
0.003?p???p??0.003?1600?4800Pa ?0.001h??
?p?4800??0.611m ??g800?9.811.12 As shown in the figure, the water level in the reservoir keeps constant. A steel drainpipe (with the inside diameter of 100mm) is connected to the bottom of the reservoir. One arm of the U-tube manometer is connected to the drainpipe at the position 15m away from the bottom of the reservoir, and the other is opened to the air, the U tube is filled with mercury and the left-side arm of the U tube above the mercury is filled with water. The distance between the upstream tap and the outlet of the pipeline is 20m.
a) When the gate valve is closed, R=600mm, h=1500mm; when the gate valve is opened partly, R=400mm, h=1400mm. The friction coefficient ¦Ë is 0.025, and the loss coefficient of the entrance is 0.5. Calculate the flow rate of water when the gate valve is opened partly. (in m3/h)
b) When the gate valve is widely open, calculate the static pressure at the tap (in gauge pressure, N/m2). le/d¡Ö15 when the gate valve is widely open, and the friction coefficient ¦Ë is still 0.025.
Figure for problem 1.12
Solution£º
(1) When the gate valve is opened partially, the water discharge is Set up Bernoulli equation between the surface of reservoir 1¡ª1¡¯ and the section of pressure point 2¡ª2¡¯£¬and take the center of section 2¡ª2¡¯ as the referring plane, then
2u12p1u2pgZ1???gZ2??2??hf,1¡ª2 £¨a£©
2?2?In the equation p1?0(the gauge pressure)
p2??HggR??H2Ogh?13600?9.81?0.4?1000?9.81?1.4?39630N/m2
u1?0Z2?0
When the gate valve is fully closed, the height of water level in the reservoir can be related to h (the distance between the center of pipe and the meniscus of left arm of U tube).
?HOg(Z1?h)??HggR
2 £¨b£©
where h=1.5m
R=0.6m
Substitute the known variables into equation b
13600?0.6?1.5?6.66m1000 22lV15V?hf,1_2?(?d?Kc)2?(0.025?0.1?0.5)2?2.13V2Z1?Substitute the known variables equation a
V2396309.81¡Á6.66=??2.13V2
21000the velocity is V =3.13m/s
the flow rate of water is
Vh?3600??4d2V?3600??4?0.12?3.13?88.5m3/h
2£© the pressure of the point where pressure is measured when the gate valve is wide-open. Write mechanical energy balance equation between the stations 1¡ª1¡¯ and 3-3¡ä£¬then
V32p3V12p1gZ1???gZ3????hf,1¡ª3 £¨c£©
2?2?since Z1?6.66m
Z3?0
u1?0 p1?p3l?leV2?hf,1_3?(?d?Kc)235V2 ?[0.025(?15)?0.5]
0.12 ?4.81V2input the above data into equation c£¬
V2?4.81V2 9.81?6.66?2the velocity is: V=3.51 m/s
Write mechanical energy balance equation between thestations 1¡ª1¡¯ and 2¡ª¡ª2¡¯, for the same situation of water level
V12p1V22p2gZ1???gZ2????hf,1¡ª2
2?2?£¨d£©
since Z1?6.66m
Z2?0
u1?0u2?3.51m/s
p1?0(page pressure£©?h
f,1_2lV2153.512?(??Kc)?(0.025??0.5)?26.2J/kg
d20.12input the above data into equation d£¬
p3.5129.81¡Á6.66=?2?26.2
21000the pressure is: p2?32970
1.14 Water at 20¡æ passes through a steel pipe with an inside diameter of 300mm and 2m long. There is a attached-pipe (¦µ60?3.5mm) which is parallel with the main pipe. The total length including the equivalent length of all form losses of the attached-pipe is 10m. A rotameter is installed in the branch pipe. When the reading of the rotameter is 2.72m3/h, try to calculate the flow rate in the main pipe and the total flow rate, respectively. The frictional coefficient of the main pipe and the attached-pipe is 0.018 and 0.03, respectively. Solution£º The variables of main pipe are denoted by a subscript1, and branch pipe by subscript 2.
The friction loss for parallel pipelines is
?hf1??hf2Vs?VS1?VS2
The energy loss in the branch pipe is
2l2??le2u2??2
d22?hf2In the equation ?2?0.03