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BernoullisLawDerivationDiagram.svg
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́ (́ ́)  , ( ) . , .

, ,   . .

( : , 0,1·) ( : , ²/,   ). , .

1011-1012 ·

.

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V , S h.

\vec{F}\propto -\frac{\vec{v} \cdot S}{h}

, , .

, , , , , - , , ( , ) , .

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, . / .

( ) , .

[]

\eta=\frac{1}{3}\langle u \rangle \langle\lambda \rangle \rho,

\langle u \rangle   , \langle\lambda \rangle . , , \rho , \langle\lambda \rangle - . ,, . , , ( ) ; , ().

, u, \sqrt{T}

[]

, ( ).

:[1]

 {\mu} = {\mu}_0 \frac {T_0+C} {T + C} \left (\frac {T} {T_0} \right )^{3/2}.

:

  • μ = (·) T,
  • μ0 = (·) T0,
  • T = ,
  • T0 = ,
  • C = , .

0 < T < 555 K 3,45 10%, .

C

[K]

T0

[K]

μ0

[ ]

120 291.15 18.27
111 300.55 17.81
127 292.25 20.18
240 293.15 14.8
118 288.15 17.2
72 293.85 8.76
370 293.15 9.82
(IV) 416 293.65 12.54
79.4 [2] 273 19 [3]

. [1] (.).

[]

[]

, , , .   :

\tau = - \eta \frac{\partial v}{\partial n},

\eta ( ) . , \eta , t «» . , -:

 \eta = C e^{w/kT}

, , . , , ; V_{M}. ,

\eta = \frac{c}{V_{M}-b},

b  . .

, .

[]

, , ,

\nu = \frac{\eta}{\rho},

. \rho  ; \eta  (. ).

(). :

1 = 12/1c = 10-6 2/c

[]

, .   ( , , ):


\sigma_{ij} = \eta \left( \frac{\partial v_i}{\partial x_j} + \frac{\partial v_j}{\partial x_i} \right),

\sigma_{i,j}  .

, . ( ) . , . .

. , , . , .

[]

(, ) - [4]:

\eta(T)=A\cdot\exp\left(\frac{Q}{R T}\right),

Q  (/), T  (), R  (8,31 /·) A  .

: Q Q_H ( ) Q_L ( ). , \left(Q_H - Q_L\right)<Q_L, , \left(Q_H - Q_L\right)\geq Q_L. R_D=\frac{Q_H}{Q_L}: R_D<2, R_D\ge 2.

:

\eta(T)=A_1\cdot T\cdot \left[1+A_2\cdot\exp\frac{B}{R T}\right]\cdot\left[1+C\exp\frac{D}{R T}\right]

A_1, A_2, B, C D, .

T_g VTF .

T<T_g,

\eta(T)=A_LT\cdot\exp\left(\frac{Q_H}{R T}\right),

Q_H = H_d + H_m, H_d  , , H_m  . , T<T_g .

T\gg T_g

\eta(T)=A_HT\cdot\exp\left(\frac{Q_L}{R T}\right),

Q_L = H_m. , T\gg T_g , .

[]

, (. ) :

 \mu_r = \frac{\mu}{\mu_0},

μ  ; μ0  .

[]

.

[]

300, 400 500 K

, , . 15.0 °C 1.78·105 /(·), 17.8 . 1.78·105 ...

[]

(Liquid Water) (Vapor)

8.90 × 104 · 25 °C.
T (K): (·) = A × 10B/(TC)
A=2.414 × 105 ·; B = 247.8 K ; C = 140 K.

.

[°C]

[·]

10 1.308
20 1.002
30 0.7978
40 0.6531
50 0.5471
60 0.4668
70 0.4044
80 0.3550
90 0.3150
100 0.2822

[]

:

100 , [·]
0 °C (273 K) 27 °C (300 K)
17.4 18.6
8.4 9.0
20.0
22.9
21.2 23.2
15.0
11.2
9.5
25 °C
:

[·]

[·]

3.06·10-4 0.306
6.04·10-4 0.604
( 37 °C) (34)·10-3 34
0.985 985
1.3806 1380.6
1.074·10-3 1.074
1.61·10-2 16.1
( 20 °C) 1.49 1490
2.022 2022
1.526·10-3 1.526
5.44·10-4 0.544
SAE 10 ( 20 °C) 0.065 65
SAE 40 ( 20 °C) 0.319 319
1.863·10-3 1.863
( 77K) 1.58·10-4 0.158
1.945·10-3 1.945
.081 81
2.42·10-2 24.2
8.94·10-4 0.894

[]

  1. Alexander J. Smits, Jean-Paul Dussauge Turbulent shear layers in supersonic flow, Birkhäuser, 2006, ISBN 0-387-26140-0 p. 46
  2. data constants for sutherland's formula
  3. Viscosity of liquids and gases
  4. . . . . , , 1975., . 226

[] .

[]

  • ., , № 9, 1983.
  •   .
  • R.H. Doremus. J. Appl. Phys., 92, 7619-7629 (2002).
  • M.I. Ojovan, W.E. Lee. J. Appl. Phys., 95, 3803-3810 (2004).
  • M.I. Ojovan, K.P. Travis, R.J. Hand. J. Phys.: Condensed Matter, 19, 415107 (2007).
  • . .  . ., .
  • .
  • .. , 1

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