Respuesta :
Answer:
5
Explanation:
Given:-
- The power dissipated by a transistor, q = 6 W
- The dimensions of the plate: ( 25 x 25 ) cm
- The forced velocity of air, V = 4 m/s
- The temperature of the air, T∞ = 35°C
- The temperature of the surface, Ts = 65°C
Declare Variables/Symbols:
- The number of transistors used = n
- Thermal conductivity = k
- Prandlt Number = Pr
- Nusselt Number ( averaged ) = Nu*
- Heat transfer coefficient ( averaged ) = h*
- Reynold's Number = Re
- Critical Reynold's Number ( Re,c ) = 5*10^5
- Density = ρ ( kg/m^3 )
- Dynamic Viscosity = μ ( kg/m.s )
Find:-
Assuming the heat transfer from the back side of the plate to be negligible and disregarding radiation, determine the number of transistors that can be placed on this plate
Solution:-
- We will perform the heat balance on the system ( aluminium plate integrated with transistors ). We will ignore the radiation effects and only consider the forced convective cooling of the transistors subjected to a stream of air forced at V = 4 m/s over the plate.
- From heat balance the rate at which heat is dissipated from the circuit -board is:
[tex]n*q = h^*.A_s.( T_s - T_i_n_f )[/tex]
Where,
h*: The average heat transfer coefficient over the edge of the plate
As: The area exposed to convective current
- We need to determine the average heat transfer coefficient ( h* ) over the flat plate for the given conditions. We know that the heat transfer coefficient is a function of a dimensionless quantity ( Nu* ), thermal conductivity ( k ) of convection fluid and edge length of the plate ( L ).
- We will first determine the thermo-physical properties of the convective fluid ( air ). Its a standard practise to evaluate these properties at the film temperature ( T ) , i.e the average of surface temperature ( Ts ) and the free stream temperature ( T∞ ). Thus,
[tex]T_f = \frac{T_s + T_i_n_f}{2} = \frac{65 + 35}{2}\\\\T_f = 50[/tex]
- Use thermo-physical tables ( A - 4 ) and evaluate properties at T = 50°C:
k = 0.02735 W /m.K
Pr = 0.7228
ρ = 1.092 kg/m^3
μ = 1.963*10^-5 kg/m.s
- The average Nusselt Number ( Nu* ) is a function of flow properties of the convective fluid namely: ( Re , Pr ). We will determine the Reynold's number over the edge of the aluminium plate as follows:
[tex]Re_L = \frac{p*V*L}{u} = \frac{1.092*4*0.25}{1.963*10^-^5} = 55629.1391[/tex]
- The Reynold's number define the flow conditions of the fluid. We see that Reynold number calculated above is within the critical Reynold's number ( Re,c ). Therefore,
Re = 5.6 * 10^5 ≤ Re,c ( 5*10^5 )
- For flows with Re < Re,c, we take the assumption of "Laminar Boundary Layer".
- The corresponding (averaged) Nusselt Number empirical relation for Laminar flow regime and constant surface temperature ( Ts = 65°C ) over flat plate ( forced convection) we have:
[tex]Nu^* = 0.664. Re_L^\frac{1}{2}. Pr^\frac{1}{3}\\\\Nu^* = 0.664. (55629.13907)^\frac{1}{2}. (0.7228)^\frac{1}{3}\\\\Nu^* = 140.5482[/tex]
- From above relation we can evaluate the average heat transfer coefficient ( h* ) as follows:
[tex]h^* = \frac{Nu_L^*. k}{L} = \frac{140.5482. 0.02735}{0.25}\\\\h^* = 15.376 \frac{W}{m^2.K}[/tex]
- Now we can use the energy balance applied to the system initially developed and solve for ( n ):
[tex]n = \frac{h^*. A_s. ( Ts - T_i_n_f)}{q} \\\\n = \frac{15.376. ( 0.25)^2 . ( 65 - 35)}{6} \\\\n = 4.8[/tex]
Answer: The number of transistors that can be placed are 5.
Note: In the above evaluation we have made an assumption that the exposed area ( As ) is equivalent to the surface area of the aluminium plate. This neglects the area associated with the thickness of the transistors. Moreover, we have assumed that the back-side of plate is thermally insulated. Also the surface temperature ( Ts ) of the plate base and the top of the transistor is assumed to be similar (if not then, we would have applied extended fin analysis ).