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Principles of
Convection
Physical
Mechanism of
Convection
 Convection vs conduction
 Heat in liquids and gases
 Speed of heat transfer because of the motion of molecules
 Convection heat transfer depends on: - fluid properties dynamic
viscosity - thermal conductivity - density - specific heat - fluid
velocity - geometry and the roughness of the solid surface - the
type of fluid flow (such as being streamlined or turbulent).
 𝑄𝑐𝑜𝑛𝑣 = ℎ𝐴𝑠 𝑇𝑠 − 𝑇∞ 𝑊 - Newton’s law of cooling
 Convection heat transfer coefficient, h
 No – slip condition
 Velocity profiles
 No – temperature jump condition
 Pure conduction at solid fluid surface
 Convection heat transfer coefficient (cond. & conv.)
Nusselt
Number
 Nusselt number represents the enhancement of heat transfer
through a fluid layer as a result of convection relative to
conduction across the same fluid layer.

𝑞𝑐𝑜𝑛𝑣
𝑞𝑐𝑜𝑛𝑑
=
ℎ∆𝑇
𝑘∆𝑇 𝐿
=
ℎ𝐿
𝑘
= 𝑁𝑢
 < 𝑁𝑢 – effectiveness of convection
 Nu = 1 – pure conduction
 Heat flux, 𝑞 - the rate of heat flow per unit time per unit surface
area
Classification
of Fluid Flows
 Viscous versus Inviscid Flow
 Internal versus External Flow – open-channel flow
 Compressible versus Incompressible Flow
 Laminar versusTurbulent Flow
 Natural (or Unforced) versus Forced Flow
 Steady versus Unsteady (Transient) Flow
 One-,Two-, andThree-Dimensional Flows
Velocity
Boundary
Layer
 Velocity boundary layer is the region of the flow above the plate
bounded by a layer of thickness in which the effects of the viscous
shearing forces caused by fluid viscosity are felt.
 Upstream velocity
 Free stream velocity 𝑢∞
 Fluid velocity, u
 No – slip condition
 Boundary layer thickness, 𝛿: 𝑢 = 0.99𝑢∞
 Boundary layer region
 Inviscid flow region
Surface Shear
Stress
 Shear stress, 𝜏 – friction force per unit area.
 Newtonian fluids e.g. water, gasoline vs non-Newtonian fluids e.g.
blood, plastic fluids
Surface shear stress, 𝜏𝑠 = 𝜇
𝜕𝑢
𝜕𝑦 𝑦=0
(𝑁 𝑚2
) where 𝜇 – dynamic
viscosity of the fluid (𝑘𝑔 𝑚 . 𝑠)
 Kinematic viscosity, 𝜈 =
𝜇
𝜌
(𝑚2 𝑠) where 𝜌 - density
 Viscosity is a measure of a fluid’s resistance to flow, its related to
temperature (liquids and gases)
 Surface shear stress vs velocity profile (friction coefficient,
upstream velocity, friction force, surface area)
TheThermal
Boundary
Layer
 Thermal boundary layer develops when a fluid at a specified
temperature flows over a surface that is at a different
temperature
 Thermal boundary layer, 𝛿𝑡 - is the distance from the surface
at which the temperature difference 𝑇 − 𝑇𝑠 = 0.99(𝑇∞ − 𝑇𝑠) .
 𝑇𝑠 = 0; 𝑇 = 0.99𝑇∞vs velocity boundary layer (𝑢 = 0.99𝑢∞)
 Thickness of layer increases with flow direction
 Boundary layer and convection heat transfer
 Velocity boundary layer andThermal boundary layer
Prandtl
Number
 Prandt number describes the relative thickness of the velocity and
thermal boundary layers
 𝑃𝑟 =
𝑀𝑜𝑙𝑒𝑐𝑢𝑙𝑎𝑟 𝑑𝑖𝑓𝑓𝑢𝑠𝑖𝑣𝑖𝑡𝑦 𝑜𝑓 𝑚𝑜𝑚𝑒𝑛𝑡𝑢𝑚
𝑀𝑜𝑙𝑒𝑐𝑢𝑙𝑎𝑟 𝑑𝑖𝑓𝑓𝑢𝑠𝑖𝑣𝑖𝑡𝑦 𝑜𝑓 ℎ𝑒𝑎𝑡
=
𝜐
∝
=
𝜇𝐶𝑝
𝑘
 Pr = 1 – gases
 Pr << 1 – liquid metals
 Pr >> 1 – oils
 Thermal boundary layer vs velocity boundary layer
Laminar and
Turbulent
Flows
 Laminar vs turbulent flow
 Characteristics of lamina flow
 Smooth streamlines – no
velocity fluctuations
 Highly ordered motion
 Characteristics of turbulent
flow
 Velocity fluctuations
 Highly disordered motion
 Transition
 Velocity profile (lamina/turbulent)
 Turbulent boundary layer
(laminar sub layer, buffer layer
and turbulent layer)
 Turbulent flow – heat +
momentum – friction –
convection heat transfer
 Design of heat transfer
coefficients - cost say pumps
Reynolds
Number
 Reynolds number is the ratio of inertia forces to vicious forces
(upstream velocity, characteristic length, kinematic viscosity
 Factors affecting transition from lamina to turbulent flow: -
surface geometry - surface roughness – free stream velocity -
surface temperature – type of fluid
 Re >
 Re <
 Inertia forces vs viscous – turbulence vs lamina
 Critical Reynolds number, 𝑅𝑒𝑐𝑟
Ref:
 Yunus A. Cengel, (2000). HeatTransfer,A PracticalApproach,
Second Edition.

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4. Principles of Convection.pptx

  • 2. Physical Mechanism of Convection  Convection vs conduction  Heat in liquids and gases  Speed of heat transfer because of the motion of molecules  Convection heat transfer depends on: - fluid properties dynamic viscosity - thermal conductivity - density - specific heat - fluid velocity - geometry and the roughness of the solid surface - the type of fluid flow (such as being streamlined or turbulent).  𝑄𝑐𝑜𝑛𝑣 = ℎ𝐴𝑠 𝑇𝑠 − 𝑇∞ 𝑊 - Newton’s law of cooling  Convection heat transfer coefficient, h  No – slip condition  Velocity profiles  No – temperature jump condition  Pure conduction at solid fluid surface  Convection heat transfer coefficient (cond. & conv.)
  • 3. Nusselt Number  Nusselt number represents the enhancement of heat transfer through a fluid layer as a result of convection relative to conduction across the same fluid layer.  𝑞𝑐𝑜𝑛𝑣 𝑞𝑐𝑜𝑛𝑑 = ℎ∆𝑇 𝑘∆𝑇 𝐿 = ℎ𝐿 𝑘 = 𝑁𝑢  < 𝑁𝑢 – effectiveness of convection  Nu = 1 – pure conduction  Heat flux, 𝑞 - the rate of heat flow per unit time per unit surface area
  • 4. Classification of Fluid Flows  Viscous versus Inviscid Flow  Internal versus External Flow – open-channel flow  Compressible versus Incompressible Flow  Laminar versusTurbulent Flow  Natural (or Unforced) versus Forced Flow  Steady versus Unsteady (Transient) Flow  One-,Two-, andThree-Dimensional Flows
  • 5. Velocity Boundary Layer  Velocity boundary layer is the region of the flow above the plate bounded by a layer of thickness in which the effects of the viscous shearing forces caused by fluid viscosity are felt.  Upstream velocity  Free stream velocity 𝑢∞  Fluid velocity, u  No – slip condition  Boundary layer thickness, 𝛿: 𝑢 = 0.99𝑢∞  Boundary layer region  Inviscid flow region
  • 6. Surface Shear Stress  Shear stress, 𝜏 – friction force per unit area.  Newtonian fluids e.g. water, gasoline vs non-Newtonian fluids e.g. blood, plastic fluids Surface shear stress, 𝜏𝑠 = 𝜇 𝜕𝑢 𝜕𝑦 𝑦=0 (𝑁 𝑚2 ) where 𝜇 – dynamic viscosity of the fluid (𝑘𝑔 𝑚 . 𝑠)  Kinematic viscosity, 𝜈 = 𝜇 𝜌 (𝑚2 𝑠) where 𝜌 - density  Viscosity is a measure of a fluid’s resistance to flow, its related to temperature (liquids and gases)  Surface shear stress vs velocity profile (friction coefficient, upstream velocity, friction force, surface area)
  • 7. TheThermal Boundary Layer  Thermal boundary layer develops when a fluid at a specified temperature flows over a surface that is at a different temperature  Thermal boundary layer, 𝛿𝑡 - is the distance from the surface at which the temperature difference 𝑇 − 𝑇𝑠 = 0.99(𝑇∞ − 𝑇𝑠) .  𝑇𝑠 = 0; 𝑇 = 0.99𝑇∞vs velocity boundary layer (𝑢 = 0.99𝑢∞)  Thickness of layer increases with flow direction  Boundary layer and convection heat transfer  Velocity boundary layer andThermal boundary layer
  • 8. Prandtl Number  Prandt number describes the relative thickness of the velocity and thermal boundary layers  𝑃𝑟 = 𝑀𝑜𝑙𝑒𝑐𝑢𝑙𝑎𝑟 𝑑𝑖𝑓𝑓𝑢𝑠𝑖𝑣𝑖𝑡𝑦 𝑜𝑓 𝑚𝑜𝑚𝑒𝑛𝑡𝑢𝑚 𝑀𝑜𝑙𝑒𝑐𝑢𝑙𝑎𝑟 𝑑𝑖𝑓𝑓𝑢𝑠𝑖𝑣𝑖𝑡𝑦 𝑜𝑓 ℎ𝑒𝑎𝑡 = 𝜐 ∝ = 𝜇𝐶𝑝 𝑘  Pr = 1 – gases  Pr << 1 – liquid metals  Pr >> 1 – oils  Thermal boundary layer vs velocity boundary layer
  • 9. Laminar and Turbulent Flows  Laminar vs turbulent flow  Characteristics of lamina flow  Smooth streamlines – no velocity fluctuations  Highly ordered motion  Characteristics of turbulent flow  Velocity fluctuations  Highly disordered motion  Transition  Velocity profile (lamina/turbulent)  Turbulent boundary layer (laminar sub layer, buffer layer and turbulent layer)  Turbulent flow – heat + momentum – friction – convection heat transfer  Design of heat transfer coefficients - cost say pumps
  • 10. Reynolds Number  Reynolds number is the ratio of inertia forces to vicious forces (upstream velocity, characteristic length, kinematic viscosity  Factors affecting transition from lamina to turbulent flow: - surface geometry - surface roughness – free stream velocity - surface temperature – type of fluid  Re >  Re <  Inertia forces vs viscous – turbulence vs lamina  Critical Reynolds number, 𝑅𝑒𝑐𝑟
  • 11. Ref:  Yunus A. Cengel, (2000). HeatTransfer,A PracticalApproach, Second Edition.