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- Examples of external data I can use to support the claim that the consumers living within regions with hot climate will buy the stainless steel pan with digital thermometer reading that is powered by the heat generated while cooking and that sales will be higher in summer.Solution on all other sites including this site are wrong Only attempt if previously not attempted. Answer part a and b A) Among the nondimensional numbers, in free convection, average Nusselt number depends on only Grashof and Prandtl numbers. only Grashof number. Rayleigh number. Reynolds number. B) For ideal gases, the specific heat capacity at constant pressure, thermal conductivity, dynamic viscosity, and Prandtl number are independent of pressure. How will the ratio of thicknesses of velocity boundary layer and thermal boundary layer change if pressure is increased from 1 atm to 5 atm for the flow of an ideal gas over a flat plate? We need to know the actual fluid properties to tell It will remain the same. It will decrease by a factor of 5. It will increase by a factor of 5.2.2: Water at a temperature of T∞= 25°C flows over one ofthe surfaces of a steel wall (AISI 1010) whose temperatureis Ts,1= 40°C and thermal conductivity of steel is 671 w/m.k. The wall is 0.35 m thick, and itsother surface temperature is Ts,2= 100°C. For steadystateconditions what is the convection coefficient associatedwith the water flow?
- You are designing a new eco-friendly thermal coffee mug. It is shaped like a small globe to minimize surface area, which is only about 0.04m^2. You use two 0.003m layers of recyclable PETE which has a thermal conductivity, k, of 0.2W/mK around a 0.01m layer of dead air, with a thermal conductivity of 0.026W/mK. Since this is for hot coffee, use a temperature difference of 40K. Q = Ax (T2-T1) / (R1 + R2 + etc) R =x/k. What is the heat lose through the surface in watts?B/Write down the nodal equation for an inside corner node with inside surface exposed to convection as shown in Figure (2). Insulated 129.4 137 172.9 A 132.8 200°C Fig.(1) В 103.5 45.8 67 C h = 50 W/m² 30°C Convection face m-1, n D m, n. 1 m, n F----E B Fig.(2) C n m, n-1 m 1. nYou are designing a new eco-friendly thermal coffee mug. It is shaped like a small globe to minimize surface area, which is only about 0.04m^2. You use two 0.003m layers of recyclable PETE which has a thermal conductivity, k, of 0.2W/mK around a 0.01m layer of dead air, with a thermal conductivity of 0.026W/mK. Since this is for hot coffee, use a temperature difference of 40K. Q = Ax (T2-T1) / (R1 + R2 + etc) R =x/k. A)what is the R-value for each of the two PETE layers? B) what is the R-value for the dead air? C) Which layer is the best insulator? D. What is the heat loss through the surface in Watts?
- Let's say a 3.0 gram copper wafer is dropped from a height of 50.0 meters. If 60% of the potential energy lost in the drop could be converted to thermal energy used to heat the copper from an initial temperature of 25 degrees celsius, what would the final temperature of the copper wafer? Would the answer be different if the wafer has a mass greater than 3 grams? Note: the specific heat of copper is 387 J/(kg*K). The temperature is between 25.8 and 26.0 degrees celsius, yes the bigger the mass the greater the energy. O The temperature is between 25.6 and 25.8 celsius, answer does not depend on mass. O The temperature is between 25.0 and 25.2 celsius, answer does not depend on mass. O The temperature is 25.5 and of course the more mass something has the greater energy will be needed to raise the temperature. The temperature is 26.2 and if the mass is doubled so will be the change in temperature. O The temperature is 25.9 degrees celsius and the answer does not depend on mass. O The…the hot combustion gasses of a furnace are separated from the ambient air and its surroundoing which are at 25c, by a brick wall 0.15 meter thick has a thermal conductivity of 1.2 w/(m-k) and a surface emissivity of 0.8. under steady state condition and outer surface temperature of 100c is measured. the convection heat transfer to the air adjoining this surface is characterized by a convection of 20 /(m-k), what is the inner temperature?Consider a single cylindrical fin of a uniform cross-sectional area (D = 5 mm, L = 70 mm,k = 400 W/m.K) that is attached to a wall with a base temperature of Tb = 180 C. Ambientconditions are T∞ = 50 °C and h = 210 W/m2.K.a. What is the heat transfer rate of a single fin?b. Plot the temperature distribution within the fin (Excel, MATLAB, … etc.)c. What is the material of the fin?
- A short cylinder having an initial temperature of 40 C is suddenly exposed to a convection boundary of 300 W/m².K. Use the data given below to find the tem- peratures of points A, B, C, and D. Data: k = 26 W/m-K, c, = 0.349 kJ/kg-K, p= 8,666 lbm/m'. [Ans.: Ta %3D 176 С, Тв %3D 184 С, Тс %3D 186.5 С, Т) 3D 180 C]. %3D 16 сm 6cm- B ----- -- C h T,QUESTION 2 Copper fins, 2.1 cm long and 2.1 mm in diameter, are attached to a base plate at 75 °C. A fan blows air through and around this fins at 29 °C providing an average convection coefficient of 21 W m-2 K-1. Estimate the heat dissipated through each of these fins, in milliwatt (mW). Assume negligible heat transfer though the tips. The conductivity of copper may be taken to be 400 W m-1 K-1.LTE !!:: خاص A docs.google.com Q2/ An aluminum sphere weighting 7kg and initially at a temperature of 533K is suddenly immersed in a fluid at 283K. if heat transfer coefficient between the sphere and fluid is 50W/m?.°C. Take density=2707kg/m3, specific heat=0.9KJ/kg.°C and thermal conductivity= 204W/m °C. Your answer Determine the Bi number 0.00696 0.000696 0.0052 0.00052 Other: Determine the time required to cool sphere to 263K. * 26.28min 262.8min 52.56 min 525.6 min Other: 2 Request edit access Submit