unsteady-state heat conduction

25
UNSTEADY-STATE HEAT CONDUCTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi ations where rate/duration of heating/coolin is a Design Parameter……

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UNSTEADY-STATE HEAT CONDUCTION. P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi. Applications where rate/duration of heating/cooling is a Design Parameter……. Measurement of Gas temperature. T 1. T 2 > T 1. T 2. When to record the Gas temperature?. - PowerPoint PPT Presentation

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Page 1: UNSTEADY-STATE HEAT CONDUCTION

UNSTEADY-STATE HEAT CONDUCTION

P M V SubbaraoAssociate Professor

Mechanical Engineering DepartmentIIT Delhi

Applications where rate/duration of heating/cooling is a Design Parameter……

Page 2: UNSTEADY-STATE HEAT CONDUCTION

Measurement of Gas temperature

T1

T2

T2 > T1

Page 3: UNSTEADY-STATE HEAT CONDUCTION

When to record the Gas temperature?

Page 4: UNSTEADY-STATE HEAT CONDUCTION

Welding Process : How to decide the Rate of Welding?

Page 5: UNSTEADY-STATE HEAT CONDUCTION

Injection Molding Process

They need you to help them estimate the time required for a part in a mold to cool to an acceptable temperature for removal.

Page 6: UNSTEADY-STATE HEAT CONDUCTION

Resin Transfer Molding Process

(1) Insert fiber preform (2) Close mold(3) Inject mixed resin/catalyst(4) Part solidifies via reaction(5) Open mold(6) Remove part

The cycle time for step (4) is approximately the same 25 minutes for parts of all sizes made by AeroForm. All other molding operations (1), (2), (3), (5) and (6) take a total of 5 minutes.

Page 7: UNSTEADY-STATE HEAT CONDUCTION
Page 8: UNSTEADY-STATE HEAT CONDUCTION
Page 9: UNSTEADY-STATE HEAT CONDUCTION
Page 10: UNSTEADY-STATE HEAT CONDUCTION

pCtxgT

tT

),(2

General Conduction Equation

pCtzyxg

zT

yT

xT

tT

):,,(

2

2

2

2

2

2

For Rectangular Geometry:

• The general form of these equations in multidimensions is:

Page 11: UNSTEADY-STATE HEAT CONDUCTION
Page 12: UNSTEADY-STATE HEAT CONDUCTION

Transient-conduction• Temperature will vary with location

within a system and with time.• Temperature and rate heat transfer

variation of a system are dependent on its internal resistance and surface resistance.

• If we have a ball with initial temperature of T0 and it is left in fluid at Te.

• Heat is transferred by convection at the surface.

• As the surface temperature decreases, heat is transferred from the center of the ball to the surface, then to the fluid.

Page 13: UNSTEADY-STATE HEAT CONDUCTION

Thermal Analysis of Cooling of Ball

Rate of Change in energy of metal ball = Rate of Heat transfer

Rate of Heat Transfer = Rate of Convection by fluid =Rate of Conduction transfer in the metal ball

dtdU :enegyin change of Rate

dt

drtrTrcd

dt

cTdVd

dtdU

R

V

0

2 ),(4

Page 14: UNSTEADY-STATE HEAT CONDUCTION

At any instant:

econv

Rrcond

R

TtRThAdr

trdTkAdt

drtrTrcd

),(,

),(40

2

•Now, if the system itself is copper or the volume is small, the temperature response within the slab is considerably different from that if it is glass or the volume is large.

•The response has to do with what is called the internal resistance of the material. •Further, if the convection coefficient is very high, then the surface temperature almost becomes identical to the fluid temperature quickly. •Alternatively, for a low convection coefficient a large temperature difference exists between the surface and the fluid. •The value of the convection coefficient controls what is known as the surface resistance to heat transfer.•Thus, the temperature variation within the system is dependent on the internal and surface resistances. •The larger internal resistance or the smaller surface resistance, the larger temperature variation within the system, and vice versa.

Page 15: UNSTEADY-STATE HEAT CONDUCTION

Total thermal resistance of the system: Rtot

T0 T

Rcond Rconv

TT0

Page 16: UNSTEADY-STATE HEAT CONDUCTION

•A Biot number is defined as:

Rrcond

conv

drtrdTkA

TtRThABi

,),(

solid

sticcharacteri

sticcharacteri

cond

conv

cond

conv

khL

LkAhA

RTTkA

TThABi

0

0

Page 17: UNSTEADY-STATE HEAT CONDUCTION

conv

cond

conv

cond

sticcharacteri

sticcharacteri

cond

conv

RR

hA

kAL

LkAhABi 1

Page 18: UNSTEADY-STATE HEAT CONDUCTION

Relationship between the Biot number and the temperature profile.

Page 19: UNSTEADY-STATE HEAT CONDUCTION

System with negligible internal resistance

For this case Bi 1.0.and the temperature profile within the body is quite uniform.

The rate of change in internal energy of the body is equal to the rate of heat taken away from the surface by convection:

TtThAdt

dVtcTd

convV )(

)(

TtThAdtcVTd

conv )(

Page 20: UNSTEADY-STATE HEAT CONDUCTION

TtThAdtdTcV conv )(

Rearranging:

dtcV

hATtT

dT conv

)(

Integrating to any time interval:

00)(

dtcV

hATtT

dT convT

T

Page 21: UNSTEADY-STATE HEAT CONDUCTION

cVhA

TTTT

0

ln

cVhA

eTTTT

0

Define, Thermal Time Constant hAcV

c

ceTTTT

0

Page 22: UNSTEADY-STATE HEAT CONDUCTION

TTTTT

0

*

cVthAtt

c *

Page 23: UNSTEADY-STATE HEAT CONDUCTION

Thermal Time Constant CVhAc

1

ththc CR

The total energy transferred in time t

Page 24: UNSTEADY-STATE HEAT CONDUCTION

surfacesolidsolid

sticcharacteri

AkhV

khLBi

The Fourier number (Fo) or Fourier modulus, named after Joseph Fourier, is a dimensionless number that characterizes transient heat conduction. Conceptually, it is the ratio of the heat conduction rate to the rate of thermal energy storage. It is defined as:

22sticcharacteristiccharacteri

sticcharacterio L

tCL

ktTCV

tL

TkA

F

Page 25: UNSTEADY-STATE HEAT CONDUCTION

Hot Rolling of Steel Sheets

1solid

sticcharacteri

khLBi