d the thickness of the boundary layer at a distance of x = 20 c
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A: Given:T=27°Cv=2 m/sμ=1.85*10-5 Kg/ms
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Q: Problem 3. Air at 20°C and 1 atm (p= 1.2 kg/m³ and u= 1.8×105 kg/(m-s)) flows at 3 m/s past a sharp…
A: (a) Calculate the Reynolds's number. Re=ρvLμ=1.2311.8×10-5=2×105<5×105so flow is laminar
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Q: The boundary layer formed as turbulent around the sphere is when ReD = 2.5*10^5 (a) Golf…
A: Re= 2.5×105Golf ball diameter, Dg= 43 mm= 0.043 mSoccer ball diameter, Ds= 222 mm= 0.222 m Note:…
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Q: 7- Air flows over a horizontal smooth flat plate at speed 14.5 m/s. The plate length is 1.5 m and…
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Q: A circular sign has a diameter of 50 cm and is subjected to normal winds up to 150 km/h at 10°C and…
A: Before solving we have to make some assumptions as follows: The flow of air is steady and…
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Q: 2-Air at 30 C over a flat plate at speed of 1.2 m/sec. Calculate the boundary layer thickness at…
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Q: 2- Air (v = 1.8×10° m/s) flows along a flat plate with a velocity of 150 km/hr. How long does the…
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Q: (b) The velocity profile in the laminar boundary layer can be approximated by the equation: 3 Us…
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Q: The velocity profile for a turbulent boundary layer over a flat plate is to be approximated by the…
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A: NOTE:- Here properties of water and air is not mentioned so, I took these at Tavg. i.e. at 75oC…
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A: Write the given data with suitable variables. v=5 m/sT∞=20 °CP=1 atmT=90 °Cd=60 cm=0.6 m100 cm1 mb=1…
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A: L= 5 m b=2 m v=4 msecρ=1.25kgm3ν=1.5×10-5 m2sec Thickness of the boundary δ in case of turbulant…
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- 650 °K hair 400°K 300°K 290°K Z777777///, エnSulacien Vair = 5m/s A Free Convection Find the air convection heae transfer knowing coefficiene Chair), that wind speed 5m/s. Surrounding ai cemp occurs is conveceian Where Too= 290OK.Why do vapor bubbles get larger in boiling water as they approach the surface? Type your detailed answer on Canvas using thermal concepts. BIUA A-IEE 33I X x, EE 2 V TT 12pt • Paragraph esc & %23 %$4 4 5 1 S F LE !! eConsider a wall of thickness 50 mm and thermal conductivity 14 W/m.K, the left side (x-0) is insulated. Heat generation (q) is present within the wall and the one dimensional steady-state temperature distribution is given by T(x) = ax +bxtc [°C] , where c 200 °C, a = -1285 °C/m , b=needs to he determined, andx is in meters. What is the heat fluxes at the right side, x = L, (kW/m )? 9, K 4L) Insulation
- Use for the ice? List all sumptions. 1.4 Consider axial flow of water in a cold tube. Write the heat conduction equation for the ice forming axisymmetrically on the inside surface of the tube. ice water 1.5 Consider two-dimensional conduction in the semi-circular cylinder shown. The cylinder is heated with uniform pe here to search 05:48 A qu) * ENG r-ny-E/-F hpA plane wall is insulated on its left side (? = 0). The wall generates energy uniformly at arate of ?̇ [W m 3⁄ ] and has thermal conductivity ?. On its right side (? = ?), the wall is exposedto a fluid at temperature ?" with convection coefficient ℎ.a) Draw a schematic of this plane wall. Make the schematic large enough that you cansketch the temperature profile within the wall after solving for it in later steps.b) Write out the full form of the Heat Diffusion Equation (HDE) in the appropriatecoordinate system for this physical scenario. Simplify the HDE and write out theappropriate boundary conditions in their general form (e.g., ?| #$% = ?& ).c) Derive an expression for the steady-state temperature distribution ?(?) within thewall. You may start from the general solution provided in Appendix C of the Bergmantextbook; or you may derive the solution directly from the differential equation andthe boundary conditions. Annotate your schematic by sketching the temperatureprofile…9:87 A moodle.nct.edu.om A picture window has dimensions of 1.05 m by 2.5 m and is made of glass 7.5 mm thick. On a winter day, the outside temperature is 25.5° C while the inside temperature is a comfortable at 16° C. (k of glass =0.095W/m.K) ((a*1.5)+(b*1.5)+(c*2.0) = 5marks) Calculate the following: a) the area of the window in square metres b) the temperature gradient (AT/Ax)in kelvin/metre b) the rate of heat lost through the window by conduction in watts/metre.kelvin II
- A convection problem has a Nusselt number equai to 10. where the contribution of diffusion is normalised and set equal to a value of 1.0. Select the correct statementis): | The ratio of advection to diffusion is 9. The ratio advection to convection is 10 The ratio of convection to diffusion is 10. The ratio advection to convection is 9. The ratio of advection to diffusion is 10.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 SubmitHeat transfer Question Please explain how to write an excel spreadsheet that will calculate the temperature at any time and any location for a cylinder that is being cooled by convection using the first 4 terms of the Fourier expansion that is a solution to the PDE. Input variables are to be Tj, Too, h, k, p, D.t Try this over a variety of Fourier numbers, some less than .2, some near 0.2, and some much greater than 0.2
- How do you get from equation 3.1.1 to 3.1.5? I understand that yoy mutiply both sides by Ui, but I'm confused on the math that is done to bring Ui into the partial derivative. Please show all intermediate steps.The wall (thickness L) of a furnace is comprised of brick material (thermal conductivity, k = 0.2 Wm¯' K'). Given that the atmospheric temperature is 0°C at both sides of wall, the density (p) and heat capacity (c) of the brick material are 1.6 gm cm³ and 5.0 J kg K¯l respectively. du Solve pc = k- subject to initial conditions as u(x,0) = x²(L – x). ốt Consider the case 2=- p² only.Q1 Passage of an electric current through a long conducting rod of radius r; and thermal conductivity k, results in uniform volumetric heating at a rate of ġ. The conduct- ing rod is wrapped in an electrically nonconducting cladding material of outer radius r, and thermal conduc- tivity k, and convection cooling is provided by an adjoining fluid. Conducting rod, ġ, k, 11 To Čladding, ke For steady-state conditions, write appropriate forms of the heat equations for the rod and cladding. Express ap- propriate boundary conditions for the solution of these equations.