Gr.3

28

description

sdfgsg

Transcript of Gr.3

Page 1: Gr.3
Page 2: Gr.3

Overall Mechanical Energy Balance

• A more useful type of mechanical balance for fluids, especially liquids, is a modification of the total energy balance to deal with mechanical energy.

• Mechanical energy involves work, kinetic energy, potential energy, and the flow work part of the enthalpy term.

• Mechanical energy is a form of energy that is either work or a form that can be directly converted to work.

Page 3: Gr.3

Kinetic Energy change

Potential Energy change

Pressure change

Sum of Friction losses

Shaft work

Note:α= 1 for turbulent flow, 0.5 for laminar flow

Page 4: Gr.3

Reynold’s Number

D

N Re

sPas

m

mDs

mm

kg

Units

.

:

2

3

If:Re < 2000, Laminar (straight flow)Re > 4000, Turbulent (eddying)

Page 5: Gr.3

Friction Loses in Expansion, Contraction, and Pipe Fittings

• Skin friction losses in flow through straight pipe are calculated by using the Fanning friction factor. However, if the velocity of the fluid is changed in direction or magnitude, additional friction loses occur. This results from additional turbulence which develops because of vortices and other factors.

Page 6: Gr.3

Methods to estimate the losses

1. Sudden enlargement losses. If the cross section of a pipe enlarges very gradually, very little or no extra losses are incurred. If the change is sudden, it results in additional losses due to eddies formed by the jet expanding in the enlarged section. The friction loss can be calculated by:

Page 7: Gr.3

Where:

exh Is the friction loss in J/kg

tcoefficien lossexpansion the

,)1( 2

2

1

A

AKex

Page 8: Gr.3

2. Sudden contraction losses. When the cross section of the pipe is suddenly reduced, the stream cannot follow around the sharp corner, and additional friction losses due to eddies occur. For turbulent flow, this is given by:

Page 9: Gr.3

tcoefficien lossn contractio theis

section downstreamor smaller in the velocity average theis

laminarfor 0.5 flow,ent for turbul 1

lossfriction theis

2

c

c

K

h

Page 10: Gr.3
Page 11: Gr.3

3. Losses in fittings and valves. Pipe fittings and valves also disturb the normal flow lines in a pipe and cause additional friction losses. In a short pipe with many fittings, the friction loss from these fittings could be greater than in the straight pipe. The friction loss from these fittings could be greater than in the straight pipe. The friction loss for the fittings and valves is given by the following equation:

Page 12: Gr.3

fitting the toleading pipe in the velocity average theis

or valve fitting for thefactor loss theis

:

1fK

where

Note: Values for Kf are given in Table 2.10-1 for turbulent flow and 2.10-2 for laminar flow.

Page 13: Gr.3

4. Frictional losses in mechanical energy balance equation. The frictional losses from the friction in the straight pipe (Fanning friction), enlargement losses, contraction losses, and losses in fittings and valves are all incorporated in the ΣF term from the mechanical energy balance equation, so that

Page 14: Gr.3

• If all velocities, v, v1, and v2 are the same,

Page 15: Gr.3

Pump Horsepower in Flow System

pump the todelivered shaft workor energy

efficiency fractional

pump by the fluid the todeliveredenergy mechanical

:

p

s

W

n

Ws

where

nWpW

Page 16: Gr.3

Friction Losses and Pump Horsepower

Hot water in an open storage tank at 82.2⁰C is being pumped at a rate of 0.379 from this storage tank. The line from the storage tank to the pump suction is 6.1m of 2-in. schedule 40 steel pipe and it contains three elbows. The discharge line after the pump is 61m of 2-in pipe and contains two elbows. The water discharges to the atmosphere at a height of 6.1m above the water level in the storage tank.

Page 17: Gr.3
Page 18: Gr.3

a. Calculate the frictional losses ΣFb. Make a mechanical energy balance and

calculate Ws of the pump in .c. What is the kW power of the pump if its

efficiency is 75%?

Page 19: Gr.3

Solution

s

m

mx

smxVelocity

mx

sPaxC

xs

xm

rate

918.21065.21

/10317.6

1065.21 Area

diameter) (inside m 0.05250or

mm 52.50 40 schedule in) D(2 A.5,Appendix on Based

.103474.02.82@ A.2,Appendix on Based

m

kg970.4C82.2 ion,interpolat Using

10317.660

min1

min379.0

24

233

24

3

3

33

Page 20: Gr.3

1

FlowTurbulent ,10279.4103474.0

)4.970)(918.2)(0525.0(

Number, sReynold' Using

5

3

3

Re

x

smkg

x

mkg

sm

mDvN

Page 21: Gr.3

Mechanical Energy Balance

02

becomesequation

)0,,(

0)()(2

1

2

22

1211

1212

21

22

s

s

WFgz

ppzv

WFpp

zzg

Page 22: Gr.3

Calculation for ΣF

1. Contraction loss- tank to pipe

kg

Jh

smxh

K

A

A

A

AK

vKh

c

c

c

c

cc

33.2

2

)/918.2(55.0

55.0)01(55.0

0 );1(55.0

)2

(

2

1

2

1

2

22

Page 23: Gr.3

2. Friction loss in 5 elbows

kg

Jh

xsm

xh

vKh

f

f

ff

965.15

52

)/918.2(75.0

elbows) of no.(2

75.0K 1,-2.10 Tableon Based

2

22

f

Page 24: Gr.3

3. Friction loss in straight pipe

kg

JF

smx

m

mF

v

D

LfF

f

x

D

D

xN

mmmL

f

f

f

47.104

2

)/918.2()

0525.0

1.67)(0048.0(4

24

0048.0

000876.00525.0

106.4

0525.0

10279.4

1.67611.6

2

22

5

5Re

Page 25: Gr.3
Page 26: Gr.3

• For ΣF

kg

JF

kg

JF

FhhF ffc

77.122

)47.104965.1523.2(

Page 27: Gr.3

• For shaft work:

kg

JW

W

Wkg

Jmsm

sm

WFgzv

s

s

s

s

9.186

09.186

077.122)1.6)(/81.9(2

)/918.2(

02

22

2

22

Page 28: Gr.3

• kW power of pump if efficiency is 75%

kWWkW

s

kg

kg

JkW

kg

JWp

Wp

nWpWs

s

kgm

m

kg

s

mxvm

v

m

53.117.1527

)130.6(13.249

13.249

))(75.0(85.186

130.6

)4.970)(10317.6(3

33