2.2.22 · Physics › Fluid Mechanics
Intuition The big picture
Jab fluid ek flat plate ke upar bahta hai, to ek thin boundary layer grow karta hai jahan viscosity fluid ko wall se chipka deti hai (no-slip). Door se flow U ∞ par chal raha hota hai; bilkul wall par woh zero par frozen hai. Blasius solution us sawaal ka exact (well, exactly-reduced) jawab hai: velocity profile kya hai aur yeh layer kitni moti hai?
Magic trick yeh hai: agar aap y -axis ko sahi tarah stretch karo to profile ka shape har x par same dikhta hai. Yeh ek similarity solution hai — ek universal curve poori plate describe karti hai.
Definition Boundary layer
Wall ke paas ek thin region jahan viscous forces inertial forces ke comparable hoti hain , isliye velocity 0 (no-slip) se ≈ U ∞ (free stream) tak badhti hai.
WHY hum poore Navier–Stokes equations solve nahi kar sakte? Kyunki woh brutal nonlinear PDEs hain. Prandtl ki insight (1904): ek thin layer ke andar, equations bahut zyada simplify ho jaate hain. Blasius (1908, unka PhD) ne phir us simplified set ko flat plate ke liye solve kiya.
Start karo 2D steady incompressible flow se, koi pressure gradient nahi (flat plate, ∂ p / ∂ x = 0 bahar):
Continuity:
∂ x ∂ u + ∂ y ∂ v = 0
x-momentum (Navier–Stokes):
u ∂ x ∂ u + v ∂ y ∂ u = ν ( ∂ x 2 ∂ 2 u + ∂ y 2 ∂ 2 u )
∂ 2 u / ∂ x 2
Layer thin hoti hai: δ ≪ x . Layer ke across (in y ) variation fast hoti hai; along it (in x ) variation slow hoti hai. Isliye ∂ 2 u / ∂ y 2 ≫ ∂ 2 u / ∂ x 2 . Hum sirf bada term rakhte hain.
Prandtl boundary-layer equation:
u ∂ x ∂ u + v ∂ y ∂ u = ν ∂ y 2 ∂ 2 u
boundary conditions ke saath:
u ( x , 0 ) = 0 , v ( x , 0 ) = 0 , u ( x , ∞ ) = U ∞
Intuition The scaling guess
Inertia ∼ U ∞ 2 / x ko viscosity ∼ ν U ∞ / δ 2 ke saath balance karo. Unhe equal set karne par δ ∼ ν x / U ∞ milta hai. Isliye natural "stretched" wall-distance yeh hai:
η = y ν x U ∞
η ke against plot kiye gaye profiles sab ek curve par collapse ho jaate hain.
Similarity variable aur ek dimensionless stream function f define karo:
η = y ν x U ∞ , ψ = ν x U ∞ f ( η )
Kyunki u = ∂ ψ / ∂ y aur v = − ∂ ψ / ∂ x (yeh automatically continuity satisfy karta hai — WHY hum stream function use karte hain), hum compute karte hain:
u = U ∞ f ′ ( η )
Yeh step kyun? ∂ ψ / ∂ y = ν x U ∞ f ′ ( η ) ⋅ ∂ η / ∂ y = ν x U ∞ f ′ ⋅ U ∞ / ( ν x ) = U ∞ f ′ .
v = 2 1 x ν U ∞ ( η f ′ − f )
u , v aur unke derivatives ko Prandtl equation mein substitute karne par, saare x aur U ∞ cancel ho jaate hain, aur ek pure ODE bachti hai:
Yeh ek 3rd-order nonlinear ODE hai jiska koi closed form nahi hai — numerically solve kiya jaata hai. Key numerical result:
f ′′ ( 0 ) = 0.332
Yeh step kyun (0.664 ): C f = 2 1 ρ U ∞ 2 0.332 μ U ∞ U ∞ / ν x = U ∞ x / ν 2 ( 0.332 ) = R e x 0.664 .
Worked example Example 1 — thickness of the layer
Air (ν = 1.5 × 1 0 − 5 m 2 / s ) ek plate ke upar U ∞ = 10 m/s par bahta hai. x = 0.5 m par δ nikalo.
Step 1 — Reynolds number: R e x = 1.5 × 1 0 − 5 10 × 0.5 = 3.33 × 1 0 5 . Kyun? Confirm karta hai ki laminar hai (< 5 × 1 0 5 ), isliye Blasius apply hota hai.
Step 2 — δ = R e x 5.0 x = 3.33 × 1 0 5 5.0 × 0.5 = 577 2.5 = 4.3 mm . Kyun? Boxed formula mein plug karo. Aadhe metre par 4 mm ki layer — genuinely thin ✓.
Worked example Example 2 — wall shear at a point
Same flow, x = 0.5 m par τ w nikalo. ρ = 1.2 kg/m 3 lo.
Step 1 — C f = 0.664/ R e x = 0.664/577 = 1.15 × 1 0 − 3 . Kyun? Pehle local friction coefficient — dimensionless, easy.
Step 2 — τ w = C f ⋅ 2 1 ρ U ∞ 2 = 1.15 × 1 0 − 3 × 2 1 × 1.2 × 100 = 0.069 Pa . Kyun? Dynamic pressure 2 1 ρ U ∞ 2 use karke un-normalize karo.
Worked example Example 3 — total drag
Plate length L = 0.5 m, width b = 0.2 m, same air. Ek side par drag?
Step 1 — R e L = 3.33 × 1 0 5 , C D = 1.328/ R e L = 2.30 × 1 0 − 3 . Kyun? C D averaged friction use karta hai (end par C f ka do guna).
Step 2 — F D = C D ⋅ 2 1 ρ U ∞ 2 ⋅ ( b L ) = 2.30 × 1 0 − 3 × 60 × 0.1 = 0.0138 N . Kyun? Plate area b L = 0.1 m 2 se multiply karo.
δ linearly x ke saath grow karta hai."
Kyun sahi lagta hai: layer clearly downstream moti hoti hai, isliye straight-line growth natural lagti hai.
Fix: yeh x ki tarah grow karta hai, kyunki δ ∝ ν x / U ∞ . Growth decelerate karta hai. Linear growth far downstream thickness over-predict karti.
Common mistake Turbulent flow ke liye
δ = 5.0 ν x / U ∞ use karna.
Kyun sahi lagta hai: yahi formula aapne yaad kiya tha.
Fix: Blasius sirf laminar hai (R e x ≲ 5 × 1 0 5 ). Turbulent layers x 4/5 ki tarah grow karti hain aur bahut moti hoti hain; δ / x ≈ 0.37 R e x − 1/5 use karo.
Common mistake Layer ke andar
v = 0 bhool jaana.
Kyun sahi lagta hai: "flow plate ke parallel hai."
Fix: continuity majboor karti hai ek small upward v jo layer ke thick hone par aata hai — isliye v = 2 1 ν U ∞ / x ( η f ′ − f ) = 0 . Yeh layer mein momentum carry karta hai.
Common mistake Blasius equation ko clean analytic solution wala samajhna.
Kyun sahi lagta hai: physics formulas mein usually hota hai.
Fix: f ′′′ + 2 1 f f ′′ = 0 ka koi closed form nahi hai; f ′′ ( 0 ) = 0.332 numerics (shooting method) se aata hai.
Recall Feynman: explain to a 12-year-old
Socho tum apna haath ek carpet ke bilkul upar flat rakh ke ghuma rahe ho jabki hawa upar se bahe. Bilkul carpet par hawa hilti nahi — woh stuck hai (sticky rule). Door upar, hawa freely zoom karti hai. Beech mein ek thin "slow zone" hoti hai jo carpet ke saath aage badhte hue thoda aur moti hoti jaati hai — lekin woh thicker slower aur slower hoti hai, jaise ek shadow stretch karti hai. Blasius ne exact shape nikali ki hawa kitni tezi se speed up karti hai jab tum carpet se upar jaate ho, aur unhone paya ki yeh shape hamesha same hoti hai agar tum height sahi tarike se measure karo. Unhone yeh bhi nikala ki hawa carpet par kitni drag karti hai — aur woh drag utni hi kamzor hoti jaati hai jitna tez ya lamba flow hota hai.
Mnemonic Remember the numbers
"Five thick, three-thirty drag, six-six-four friction, one-three-two-eight total."
δ : 5.0 · f ′′ ( 0 ) : 0.332 · C f : 0.664 · C D : 1.328 .
Note karo: 0.664 = 2 × 0.332 , aur 1.328 = 2 × 0.664 . Har step double hota hai.
Prandtl Navier–Stokes ko wall ke paas simplify karne ke liye kya approximation use karta hai? Layer thin hoti hai (δ ≪ x ), isliye ∂ 2 u / ∂ x 2 negligible hai ∂ 2 u / ∂ y 2 ke muqable mein.
Blasius similarity variable η define karo. Blasius ODE aur uske BCs kya hain? f ′′′ + 2 1 f f ′′ = 0 ; f ( 0 ) = 0 , f ′ ( 0 ) = 0 , f ′ ( ∞ ) = 1 .
f ′ ( η ) physically kya represent karta hai?Velocity ratio u / U ∞ .
Stream function ψ kyun use karte hain? Yeh continuity automatically satisfy karta hai (u = ψ y , v = − ψ x ).
f ′′ ( 0 ) ki value aur yeh kya control karta hai?0.332 ; wall shear stress set karta hai (wall par velocity gradient).
Boundary-layer thickness formula (99%)? δ = 5.0 x / R e x , yaani
δ ∝ x .
Local skin-friction coefficient? Length L ki plate ke ek side ka total drag coefficient? Blasius solution ki validity limit? Laminar flow, R e x ≲ 5 × 1 0 5 .
δ ka U ∞ ke saath scaling kya hai?δ ∝ 1/ U ∞ — tez flow ⇒ thinner layer.
Wall shear stress expression?
solve karna bahut mushkil
Prandtl boundary-layer eqn
No-slip and free-stream BCs
Scaling balance inertia vs viscosity
Layer thickness delta ~ sqrt of nu x over U
Stream function psi with f of eta
Blasius ODE 2f triple prime plus f f double prime equals 0