Как выбрать гостиницу для кошек
14 декабря, 2021
1.4 Governing equations.- The
fluid flow and heat transfer is assumed to be governed by the two dimensional Navier-Stokes equations, together with the energy equation, using the following restrictions: steady state, laminar flow, fluid Newtonian behaviour, Boussinesq approximations, radiatively non — participating medium and negligible both heat friction and influence of pressure on temperature. This set of differential equations are represented in Eqs. 2 — 5, where ( ) are the Cartesian — coor
dinates; T is the temperature;
T0 the reference temperature; pd the dynamic pressure; (u, v) and ( ) are and у components
of velocity and the gravitational acceleration.
The solid parts (glass sheets) are governed by the energy equation (Eq. 5) without considering convective terms.
^ + £ = 0(2) dy
■т0)дх (3)
-T0)gv (4)
Q-2JS
The governing equations can be adimensionalized using the dimensional quantities Lref = , , , and, where is the thermal
diffusivity. The following adimensional variables are obtained: , ua = ufuref,
and. The flow structure is fully described by Rayleigh and
Prandtl numbers (Ra, Pr); by the shape of the geometry (A, A’, lh/L, lc/L and S/L); and by the thermal conductivity ratio ДА.
Study III: |
Ra = 10 *, |
l/L = 0.4, H |
= 20 L |
||
Whole Domain |
Reduced Domain |
||||
A’ |
№h) |
A1 |
k |
||
2.0 |
9 |
5/3 |
5/3 |
2.0 |
5 |
1.819 |
10 |
5/3 |
5/3 |
1.819 |
5 |
1.6675 |
11 |
5/3 |
5/3 |
1.6675 |
22/5 |
1.539 |
12 |
5/3 |
5/3 |
1.539 |
4 |
1.429 |
13 |
5/3 |
4/3 |
1.429 |
18/5 |
1.334 |
14 |
4/3 |
4/3 |
1.334 |
16/5 |
1.25 |
15 |
4/3 |
4/3 |
1.25 |
16/5 |
1.177 |
16 |
4/3 |
4/3 |
1.177 |
3 |
1.1116 |
17 |
4/3 |
4/3 |
1.1116 |
3 |
1.053 |
18 |
4/3 |
1 |
1.053 |
3 |
1.0005 |
19 |
1 |
1 |
1.0005 |
13/5 |
0.9528 |
20 |
1 |
1 |
0.9528 |
12/5 |
results demonstrate that velocities Table 2: Parameters of the mesh for study III: asym — and temperatures have a periodic metrical configurations when slats are close to hot (lh/L behaviour in direction, i. e.: = 0.2 lc/L = 0.4, and ) and cold (lh/L = 0.4, lc/L
= 0.2, and ) isothermal walls.
(6)
The dynamic pressure is characterized by:
PdJ, У) = Ра{х, y + H’)+ К„ (7)
where Жр is a constant value. The Kp value is calculated from analysis of the effects of buoyancy (Kelkar [2]). In this work, it is assumed that Kp is represented by:
(8)
where T0 is the Boussinesq temperature and the bulk temperature, which were expressed by:
— ,-L |
‘ fL ‘ |
|
/ Tlvldx |
і |
1 vdx |
Jo |
Jo |