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Vocabulary and correlations for laminar flow, heat transfer, and boundary layer theory over flat plates.
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Local Drag Coefficient (Cf,x)
For laminar flow over a flat plate, it is defined by the correlation Cf,x=0.664Rex−1/2.
Average Drag Coefficient (Cˉf)
For laminar flow over the entire length of a flat plate, it is defined as Cˉf=1.328ReL−1/2.
Wall Shear Stress (τw)
The stress exerted on the fluid by the wall, calculated as τw=21ρu2Cˉf.
Power (Drag)
The energy per unit time required to overcome fluid resistance, expressed as Power=force×velocity or P=0.664ρu5/2ν1/2L1/2.
Film Temperature (Tf)
The temperature used to evaluate fluid properties in the boundary layer, calculated as the average of the wall temperature and the free stream temperature: Tf=2Tw+T∞.
Average Nusselt Number (Nu)
A dimensionless parameter for convective heat transfer across the plate length L, given by the correlation Nu=khˉL=0.664ReL1/2Pr1/3.
Heat Flux (q′′)
The rate of heat transfer per unit area, defined as q′′=hˉΔT.
Local Nusselt Number (Nux)
The dimensionless heat transfer coefficient at a specific point x, defined as Nux=0.332Pr1/3Rex1/2.
Average vs. Local Convective Coefficient
For laminar flow over a flat plate, the average convective heat transfer coefficient (hˉ) is twice the local coefficient (hx) at the end of the plate: hˉ=2hx.
Critical Reynolds Number (Recritical)
The threshold value marking the transition from laminar to turbulent flow on a flat plate, typically taken as Rex<5×105 for laminar conditions.
Boundary Layer Thickness (δ)
The distance from the wall where the fluid velocity reaches 99% of the free stream velocity, given in the notes as δ=4.92xRex−1/2.
Modified Blasius Equation
The governing equation for boundary layer flow over a surface with a power-law velocity distribution (U∞=Cxm), expressed as 2f′′′+(m+1)ff′′+2m[1−(f′)2]=0.
Similarity Variable (η)
A dimensionless coordinate used to transform partial differential equations into ordinary differential equations, defined as η=yxRex.