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Industrial Control
Behzad Samadi
Department of Electrical Engineering
Amirkabir University of Technology
Winter 2009
Tehran, Iran
Behzad Samadi (Amirkabir University) Industrial Control 1 / 7
Thermal Systems
Electrical Analogy
Type of System Electrical Thermal
T-Variable i, current q, heat flow
A-Variable v, voltage T, temperature
Resistance resistor thermal resistor
Storage (A-Type) capacitor thermal capacitor
Storage (T-Type) inductor unknown
Note that q is in units of power and no T-type thermal energy storage
has been identified.
[Ogata, 1997]
Behzad Samadi (Amirkabir University) Industrial Control 2 / 7
Heat Transfer
Conduction: Heat transfer through solid media
Behzad Samadi (Amirkabir University) Industrial Control 3 / 7
Heat Transfer
Conduction: Heat transfer through solid media
T1 − T2 =Rcq
Rc =
d
KA
d =thickness of the wall
A =area of the wall
K =thermal conductivity of the wall’s material
[Macia and Thaler, 2004]
Behzad Samadi (Amirkabir University) Industrial Control 3 / 7
Heat Transfer
Convection: Heat transfer through a fluid (liquid or gas)
Behzad Samadi (Amirkabir University) Industrial Control 4 / 7
Heat Transfer
Convection: Heat transfer through a fluid (liquid or gas)
T1 − T2 =Rhq
Rc =
d
hA
d =thickness
A =area
h =convection coefficient
[Macia and Thaler, 2004]
Behzad Samadi (Amirkabir University) Industrial Control 4 / 7
Heat Transfer
Radiation:
Behzad Samadi (Amirkabir University) Industrial Control 5 / 7
Heat Transfer
Radiation:
q =AεFσ(T4
1 − T4
2 )
A =area of the surface of the object of interest
ε =parameter descriptive of the emission of surfaces 1 and 2
σ =Stefan-Boltzman Constant
F =geometrical shape factor
T1, T2 =absolute temperatures of bodies 1 and 2
[Macia and Thaler, 2004]
Behzad Samadi (Amirkabir University) Industrial Control 5 / 7
Heat Transfer
Radiation:
q =AεFσ(T4
1 − T4
2 )
Rr =
1
AεFσ(T2
1 + T2
2 )(T1 + T2)
⇒ T1 − T2 = Rr q
[Macia and Thaler, 2004]
Behzad Samadi (Amirkabir University) Industrial Control 6 / 7
Thermal Capacitance
q =C
dT
dt
C =mcx
C =thermal capacitance of the object
m =mass of the object
cx =specific heat of material
[Macia and Thaler, 2004]
Behzad Samadi (Amirkabir University) Industrial Control 7 / 7
Macia, N. F. and Thaler, G. J. (2004).
Modeling and Control of Dynamic Systems.
Delmar Learning.
Ogata, K. (1997).
Modern Control Engineering.
Prentice Hall, 3 edition.
Behzad Samadi (Amirkabir University) Industrial Control 7 / 7

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Industrial Control Systems - Thermal Systems

  • 1. Industrial Control Behzad Samadi Department of Electrical Engineering Amirkabir University of Technology Winter 2009 Tehran, Iran Behzad Samadi (Amirkabir University) Industrial Control 1 / 7
  • 2. Thermal Systems Electrical Analogy Type of System Electrical Thermal T-Variable i, current q, heat flow A-Variable v, voltage T, temperature Resistance resistor thermal resistor Storage (A-Type) capacitor thermal capacitor Storage (T-Type) inductor unknown Note that q is in units of power and no T-type thermal energy storage has been identified. [Ogata, 1997] Behzad Samadi (Amirkabir University) Industrial Control 2 / 7
  • 3. Heat Transfer Conduction: Heat transfer through solid media Behzad Samadi (Amirkabir University) Industrial Control 3 / 7
  • 4. Heat Transfer Conduction: Heat transfer through solid media T1 − T2 =Rcq Rc = d KA d =thickness of the wall A =area of the wall K =thermal conductivity of the wall’s material [Macia and Thaler, 2004] Behzad Samadi (Amirkabir University) Industrial Control 3 / 7
  • 5. Heat Transfer Convection: Heat transfer through a fluid (liquid or gas) Behzad Samadi (Amirkabir University) Industrial Control 4 / 7
  • 6. Heat Transfer Convection: Heat transfer through a fluid (liquid or gas) T1 − T2 =Rhq Rc = d hA d =thickness A =area h =convection coefficient [Macia and Thaler, 2004] Behzad Samadi (Amirkabir University) Industrial Control 4 / 7
  • 7. Heat Transfer Radiation: Behzad Samadi (Amirkabir University) Industrial Control 5 / 7
  • 8. Heat Transfer Radiation: q =AεFσ(T4 1 − T4 2 ) A =area of the surface of the object of interest ε =parameter descriptive of the emission of surfaces 1 and 2 σ =Stefan-Boltzman Constant F =geometrical shape factor T1, T2 =absolute temperatures of bodies 1 and 2 [Macia and Thaler, 2004] Behzad Samadi (Amirkabir University) Industrial Control 5 / 7
  • 9. Heat Transfer Radiation: q =AεFσ(T4 1 − T4 2 ) Rr = 1 AεFσ(T2 1 + T2 2 )(T1 + T2) ⇒ T1 − T2 = Rr q [Macia and Thaler, 2004] Behzad Samadi (Amirkabir University) Industrial Control 6 / 7
  • 10. Thermal Capacitance q =C dT dt C =mcx C =thermal capacitance of the object m =mass of the object cx =specific heat of material [Macia and Thaler, 2004] Behzad Samadi (Amirkabir University) Industrial Control 7 / 7
  • 11. Macia, N. F. and Thaler, G. J. (2004). Modeling and Control of Dynamic Systems. Delmar Learning. Ogata, K. (1997). Modern Control Engineering. Prentice Hall, 3 edition. Behzad Samadi (Amirkabir University) Industrial Control 7 / 7