UNIVERSITY OF TORONTO DEPARTMENT OF MECHANICAL & INDUSTRIAL ENGINEERING MIE313H-Heat and Mass Transfer Laboratory Experiment β V Winter 2023 NOTES: (i) Attempt all 4 parts of the project (ii) Total mark: 100 points Name: Surname: Student #: -------------------------------------------------------------------------------------------------------------------- Objective: 1. To study the natural convection mechanism for cooling processes. 2. To analyze the multimode heat transfer. Equipment: • Energy2D simulator. Part A) Natural Convection: One of the fundamental problems of interest in convective heat transfer is cooling processes with natural convection. While the geometry could not be any more basic, as shown in Figure 1, occurs in a number of engineering applications. In this flow type, the boundary layers develop freely, without any constraints imposed by adjacent surfaces. Consequently, there will always be a region of the flow outside the boundary layer in which velocity and temperature gradients are negligible. As shown in Figure 1, the heat generated inside an aluminum wall (height=0.5 m, width=0.04 m, depth= 1m, and πΜ = 200 π⁄ 3 ) will be cool down by surrounding gas. Insulations have π surrounded the wall. Therefore, it can only transfer energy to the surrounding gas. The temperature of the surface of the wall will be measured during the process. The initial temperature of the aluminum wall is ππ = 500π πΆ . Page 1 of 4 Figure 1: Cooling of the wall with natural convection In this part, the wall is only cooled down by the natural convection mechanism with different conditions, as shown in the following Table: Gas’s Thermal Kinematic Thermal Thermal Temperature (C) Expansion Viscosity Diffusivity Conductivity (m2/s) (m2/s) (W/m.C) Coefficient (1/C) Case 1 50 0.000005 0.002 0.0001 0.02 Case 2 100 0.000002 0.0025 0.00024 0.05 Case 3 150 0.000001 0.003 0.00036 0.07 Run the “part1_case1.e2d”, “part1_case2.e2d”, and “part1_case3.e2d” files and stop the simulation once it becomes a steady state. Page 2 of 4 1-Find the average convective heat transfer coefficient (βΜ ) of different cases using the following equation (15 Points): π" = βΜ (ππ − π∞ ) (1) where π" = βπππ‘ πππ’π₯, π∞ = πππ ’π π‘πππππππ‘π’ππ , ππ = π‘πππππππ‘π’ππ ππ π‘βπ π π’πππππ ππ π‘βπ π€πππ 2- Find the coefficients a and b for the following correlation expressing the relationship between Μ Μ Μ Μ Μ Μ πΏ ) and the Rayleigh number (π ππΏ ) in a vertical cavity (35 Points): the Nusselt number (ππ’ Μ Μ Μ Μ Μ Μ ππ’πΏ = π(π ππΏ )π (2) where Μ βπΏ Μ Μ Μ Μ Μ Μ ππ’πΏ = , π ππ½(ππ − π∞ )πΏ3 π ππΏ = π£πΌ π½ = πβπππππ πΈπ₯ππππ πππ πΆππππππππππ‘ , π£ = πΎππππππ‘ππ πππ πππ ππ‘π¦ πΌ = πβπππππ π·ππππ’π ππ£ππ‘π¦ = π ππΆπ π = ππππ£ππ‘π¦ = 9.81 π/π 2 , πΏ = βπππβπ‘ ππ π€πππ Hint: By taking the natural log, equation 2 will turn into a linear equation: Μ Μ Μ Μ Μ Μ πΏ ) = πΏπ(π) + π × ππ(π ππΏ ) ππ(ππ’ Then, by determining Nusselt and Rayleigh numbers of each case, fit a linear curve and find a and b. (For Fitting you can use any software like excel, origin, etc. Also, a handout has been uploaded on Quercus which shows how to fit a curve using Python) Page 3 of 4 Part B) Multimode Heat Transfer: In this part, the same setup (an aluminum wall with of height=0.5 m, width=0.04 m, depth= 1m, and πΜ = 200 π⁄ 3) will be used to analysis the effect of radiation in the cooling process. It should π be mentioned that the initial temperature of the aluminum wall is ππ = 500π πΆ, and temperature of gas is π∞ = 0π πΆ . Consider the following scenarios in the cooling process of the wall: • The wall is only cooled down by natural convection mechanism (part2_single_mode.e2d). • In addition to natural convection, the wall can transfer energy by radiation to the surrounding walls (ππ€ππππ = 0π πΆ), (part2_multi_mode.e2d). 3- Derive the expressions for the temperature of the wall for both cases. Write down all assumptions of the expressions and initial/boundary conditions. (You may use the results of the simulations for some of your assumption) (25 Points) 4- Run the “part2_single_mode.e2d” and “part2_multi_mode.e2d” files and stop the simulation after 45 minutes of CFD time (CFD time is shown on the right corner of each simulation). Compare the temperature of the wall in both cases. What is the effect of radiation on the temperature of the wall and the rate of heat transfer? (25 Points) Page 4 of 4