The zeroth law of turbulence and its discontents
If in an experiment on turbulent flow all control parameters are fixed, except for the viscosity, which is lowered as much as possible, the energy dissipation per unit mass approaches a nonzero limit. Turbulence - the Legacy of A.N. Kolmogorov Uriel Frisch (1996) An example of the zeroth 2 law of turbulence ρ(ut + u·∇u)+∇p = µ u + f and ∇·u =0 ∇ Some equations for LANL 5 “If my views be correct, a fall of 800 feet will d generate one degree of heat, and the temperature 1 u 2 dx = u·f dx ν ω 2 dx Some equations for LANL 5 dt 2| | − | | of the river Niagara will be raised about one fifth !V !V !V of a degreegH by its1 0fall of4 1608 feet.” (Joule 1845) ∆T = = × K = 0.11K cp 4200 Wikimedia ω = ∇ u gH 10 48 × ∆T = = × K = 0.11K cp 4200 2 1 1 lim ν ω dx =0 cp = 4200JK− kg− ν 0 | | ̸ → !V (For seawater cp is close to 4000MKS) 1 1 cp = 4200JK− kg− 2 ∇ ρ ut + u·∇u + ∇p = µ u This dissipative process requires × " ∇ % molecularg H viscosity.= gα∆ ButT the1 coefficient03 6 m s 1 ′ × × ≈ − # $ !of viscosity ν! is very small and Joule 2 takes it as given, or obvious, that3 the 1 ωt + u·∇ω = ω·∇u + ν ω g′ H = gα∆T 10 6 m s− 6 2 1 × × ≈ ⌫water 10 m s ∇ ! exact value! of ν unimportant. 7 ⇡ √gHH R = 1010 νwater ∼ 7
ˆ u = uˆı + vȷωˆ =(vx uy)k ∴ ω·∇u =0 −
−5 2 −1 νair 10 m s ≈
1 That’s a great story about Joule’s honeymoon, but is it true? He did the calculation, but did he measure the temperature rise? That’s a great story about Joule’s honeymoon, but is it true? He did the calculation, but did he measure the temperature rise?
• The temperature increase, 0.1degree, is smaller than the expected variation of air temperature over H=50m. (For example, the average tropospheric lapse rate is 6.6 degrees per kilometer.) • But is the water in thermal equilibrium with atmosphere? • What about air drag on falling drops, and evaporative cooling of spray? • The temperature increase is buried in a lot of noise and the story is probably apocryphal…..
(Craig Bohren, American Journal of Physics) Another example
5 1 ⌫ 10 ms air ⇡ R 106 ⇠
1 UL Drag = C (R)⇥AU 2 with R = 2 D
and lim CD(R) is non-zero R !1 102 1 2 3 W = CD ρ L U 101 Stokes flow 2
CD CD( ) =0 100 1 6 Frisch(1996)
“Turbulence” Uriel “Turbulence” 10-1 10-1 100 101 102 103 104 105 106 107 R = L U/ν
The drag coefficient means the limit at infinite Reynolds number.
There is no drag without viscosity, but ultimately the value of ν is irrelevant. ν→0 is a singular limit.
From Wikipedia From This is the zeroth law of turbulence. D’Alembert’s paradox “The theory (potential flow), developed in all possible rigor, gives, at least in several cases, a strictly vanishing resistance, a singular paradox which I leave to future Geometers” D’Alembert
“Fluid mechanics is divided between hydraulic engineers who observe phenomena which cannot be explained and mathematicians who explain phenomena which cannot be observed.” Cyril Hinselwood
The zeroth law of turbulence If in an experiment on turbulent flow all control parameters are fixed, except for the viscosity, which is lowered as much as possible, the energy dissipation per unit mass approaches a nonzero limit. “Turbulence - the Legacy of A.N. Kolmogorov” Uriel Frisch (1996) An enclosed incompressible fluid ˆ ∇ u = k ψ 2 × ρ(ut + u·∇u)+∇p = µ∇ u + f and ∇·u =0 2 ρ(ut + u·∇u)+∇p = µ∇ u + f and and ∇·u =0 2 ρ(ut + u·∇u)+∇p = µ∇ u + f and ∇·u =0 u 2 2 =0 ρ(ut + u·∇ρ(uudt)++ u∇1·p∇=u2 )+µ∇∇up+=fµ∇ u + fand 2 and∇·u =0∇·u =0 2|u| dx = u·f dx − ν |ω| dx d dt V V V 1|u|2 dx = u·f dx −Theν power|ω|2 d xintegral! is: ! ! 2 d 2 2 dt V V V 1|u| dx = u·f dx − ν |ω| dx d ! 1 2 ! !d 2 1 2d 2 2 ∇ψ x y ν ζ x y dt 1V 2 ·ω = ∇ ×V·u V 2 2 d d = d2|ud| dx =!2|u| udxf =dx −!uν f d|xω|−dνx !|ω| dx dt !! | | − !!dt V dt V V V V V ω = ∇ × u ! ! ! ! ! ! with the vorticitylim ν |ωω|2 d=x ̸=0∇ × u ν→0 V d 1 2 2 ω = ∇ ×!ωu = ∇ × u ζ dxlimdyν =|ω|2 dνx ̸=0 ∇ζ dxdy 2 ν→0 V dt !! ! − !! | | lim ν |ω|2 dx ̸=0 ν→0 2 ∇ × ρ ut + 2u·∇u +V ∇p = µ∇ u lim ν |ω| dx ̸=0 ! 2 ν→0 V The 2zeroth law" is:! lim ν |ω| dx ̸=0 % ∇ × ρ ut + u·∇u + ∇p = µ∇ u # ν→0 $ d 2 ′′ !V 2 " ∇ % ∇ × ρ ut + u·∇u + ∇2p = µ∇ u F (ζ)dxdy = ν ζ F (ζ)dx ·∇ ·∇ 2 dt !! # − $!! | | ∇ ρ uωt +u·u∇"uω =∇ωp uµ + νu∇ ω % × Turbulence∇t + is+ a singular·∇= ∇ limit∇ 2 2 " × ρ u#t + u u +$ p%= µ∇ u ωt + u·∇ω = ω·∇u + ν∇ ω # (a “dissipative" $ anomaly”). 2 % ω#t + u·∇ω =$ω·∇u + ν∇ ω 2 ·∇ ·∇ 2 ˆ vx uy = ψ u = uωˆıt++vuȷωˆ ω = ω =(uv+x −ν∇uyω)k 2 ∴ ω·∇u =0 ωt + u·∇ω = ω·∇u + ν∇ ω − ∇ ˆ u = uˆı + vȷωˆ =(v − u )k ∴ ω·∇u =0 x y ˆ u = uˆı + vȷωˆ 10−5 m=(2 s−v1 x − uy)k ∴ ω·∇u =0 ˆ ˆ νair ≈ ˆ u2 = uı + vȷω=(vx − uy)k ˆ∴ ω·∇u =0 −5 2 −1 ˆ ˆ ∴ ·∇ vxνair ≈u10y =m s ψ u = uı + vȷω=(vx − uy)k ω u =0 − ∇ −5 2 −1 νair ≈ 10 m s −5 2 −1 νair ≈ 10 m s −5 2 −1 νair 10 m s d ≈1 1 u 2 dx = u·f dx ν ω 2 d 2 1 dt !V | | !V − !V | | 1 1 1 U 3 ε RMS ∼ L
1 4 ν3 / ℓK = ε ! " u =0
d 1 ∇ψ 2 dxdy = ν ζ2 dxdy dt 2 | | − ## ## −18 1/4 coffee 10 −4 ℓK = =10 m 10−2 ! " Injection scale L 3D turbulent
ε 2 energy cascade3 URMS 3 1/4 W L ε ν ∼ 3L dimℓK = ε = = URMS ε 3 ε ! " Big whorls have∼ Llittle1/4 whorls kg T ν3 u =0 Which feedℓK on= their1 velocity,4 νε3 / −183 1/4 And little whorlsℓK = have! "lesser whorls ε oceand 1 102 URMS 2 −3 ! " 2 ∇ψ dxdy = ν ζ dxdy And so on to viscosity. ℓK dt=ε| | − =5.56 10 ε =mν [ 1 (u + u )]2 (1) ## −9 ## 2 —i,j uL.=0 F.j,i Richardson ∼10 −18 L1/4 × = ν u2 + u2 + u2 + + w2 (2) coffee 10 −4 # x y z $ z ℓK != −2 "=10 m ⟨ ··· ⟩ 10 d 1 2 2 Inertialcascade ! " Yet again 2 ∇ψ dxdy = ν ζ dxdy d 1 2 W3 L2 1/4 d2t | | ¯ − ε ∇ ## κ ∆b(0) ## 2 ζ dimdx=dy == 3 ν ζ dxdy ε νkg T −≤18 1/H4 dt − | | coffee 10 −5 ℓK = −18 1/4 ℓAside:K = why turbulence=3 10 in am ##ocean 10 −##3 d 1 21 × 2 ℓK = −9 ε=5.56 10 m coffee ∇cup!ψ isdx “stronger”"dy = ν thanζ dx dy 10 × dt 2 | | − d ! !" " 2 ′′ %%turbulence in the ocean.%% d L F ζ 1 x2 y ν 2 ∇ζ F ζ x −y 1/4 ( )d2 ζ ddxdy ==ν ∇ζ dxdy ( )d d 18 dt − | | coffee 10 −5 dt ## ##− | | ℓK = =62 10 m ## uε =0 ## 0.1 W L × d ∇ 2 ′′ dim! ε =" = 3 1 F (ζ)dxdy = ν ζ F (ζ)dxdy kg T