heat transfer i p pt. (hafiz luqman)
TRANSCRIPT
These are defined as those numbers which have
no dimensions.
These are pure numbers.
For Example:
Grashof Number (Gr)
Biot Number (Bi)
Nusselt Number (Nu)
Prandtl Number (Pr) etc.
1. GRASHOF NUMBER:
The Grashof number Gr is a measure of the
relative magnitudes of the buoyancy force and the
opposing viscous force acting on the fluid.
Gr = gβ ( Ts-T∞ )Lc3 / υ2
Flow regime of heat in forced convection is
governed by Renold Number (Re) but in natural
convection it is governed by Grashof Number (Gr).
• The Grashof number provides the maincriteria in determining whether the fluid flow islaminar or turbulent in natural convection.
• For vertical plates, for example, the criticalGrashof number is observed to be about 109.Therefore, the flow regime on a vertical platebecomes turbulent at Grashof numbers greaterthan 109. When a surface is subjected toexternal flow, the problem involves bothnatural and forced convection. The relativeimportance of each mode of heat transfer is
determined by the value of the coefficient
GrL /ReL2.
• Natural convection effects are negligible if
GrL /ReL2 << 1, forced convection dominates.
Forced convection effects are negligible if
GrL /ReL2 >> 1, free convection dominates.
• Both effects are equally significant and must
be considered if GrL /ReL2 ≈ 1.
• It is used to calculate heat transfer in
natural convection, where fluid velocity
depends on buoyancy.
2. BIOT NUMBER:
“Biot number (Bi) is the index of the ratio of heattransfer resistances inside and at the surface of abody.”
It is a dimensionless number used in heat transfercalculations. It is named after the French PhysicistJean-Baptiste Biot (1774–1862).
• The Biot number is defined as:
Where,
• h = film coefficient or heat transfer coefficient or convective heat transfer coefficient
• LC = characteristic length, which is commonly defined as the volume of the body divided
by the surface area of the body, such that
• kb = Thermal conductivity of the body.
• The metal sphere may be large, causing the characteristic length to increase to the point that the Bi > 1 Now, thermal gradients within the sphere become important, even though the sphere material is a good conductor.
• Equivalently, if the sphere is made of a thermally insulating (poorly conductive) material, such as wood or styrofoam, the interior resistance to heat flow will exceed that of the fluid/sphere boundary, even with a much smaller sphere. In this case, again, the Bi > 1
• Values of the Bi < 1 imply that the heatconduction inside the body is much fasterthan the heat convection away from itssurface, and temperature gradients arenegligible inside of it.
• The Biot number has a variety of applications,including transient heat transfer and use inextended surface heat transfer calculations.
3. NUSSELT NUMBER
“Nusselt Number (Nu) the ratio between total heattransfer in a convection dominated system and theestimated conductive heat transfer.”
In convection studies, it is common practice to nondimensionalize the governing equations andcombine the variables, which group together intodimensionless numbers in order to reduce thenumber of total variables. It is also commonpractice to non dimensionalize the heat transfercoefficient h with the Nusselt number, defined as,
Nu = h×L c / k
q conv = h ∆T
and
q cond = k ∆T / L
Taking their ratios give
q conv / q cond = h ∆T/ (k ∆T / L)
= hL / k
which is the Nusselt number (Nu).
• The Nusselt Number (Nu)represents the enhancement of heat transfer through a fluid layer as a result of convection relative to conduction across the same fluid layer. The larger the Nusselt Number, the more effective the convection.
• A Nusselt Number of Nu = 1 for a fluid layer represents heat transfer across the layer by pure conduction.