1 / 44

HW # 5 /Tutorial # 5 WWWR Chapter 20 ID Chapters 7-9

Tutorial # 5 WWWR #20.5, 20.12, 20.13, 20.41, 20.42. To be discussed during the week 17 Feb. – 21 Feb., 2014. By either volunteer or class list. Homework # 5 (Self practice) . WWWR #20.6, 20.43, 20.45. ID# 7.24, 7.35.

dirk
Download Presentation

HW # 5 /Tutorial # 5 WWWR Chapter 20 ID Chapters 7-9

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript

  1. Tutorial # 5 WWWR #20.5, 20.12, 20.13, 20.41, 20.42. To be discussed during the week 17 Feb. – 21 Feb., 2014. By either volunteer or class list. Homework # 5 (Self practice). WWWR #20.6, 20.43, 20.45. ID# 7.24, 7.35. Correction: #20.42: Table: Unit for Cp should be corrected from J/kg-K to kJ/kg-K. HW # 5 /Tutorial # 5WWWR Chapter 20ID Chapters 7-9

  2. Convective Heat Transfer Correlations

  3. Natural Convection

  4. Horizontal Plates McAdam’s Correlations: Hot surface facing up or cold surface surfacing down H C C H

  5. Horizontal Cylinders g

  6. q A = h(T1 - T2) In each of the correlations to follow the temperature of the hotter of the two large surfaces is designed in T1, and the cooler surface is at temperature T2. Fluid properties are evaluated at the film temperature, Tf = (T1 + T2) / 2. Convective heat flux is expressed as

  7. Example 1

  8. H H

  9. Initial Guess T = 385K, Resulting T=381.1K  Second Iteration

  10. Forced Convection For Internal Flow

  11. Turbulent Flow

  12. Example 2 Hydraulic fluid (MIL-M-5606), in fully developed flow , flows through a 2.5 cm diameter copper tube, with a mean velocity of 0.05 m/s. The oil enters at 295K. Steam condenses on the outside tube surface with an effective heat transfer coefficient of 11400 W/m2-K. Find the rate of heat transfer to the oil. Ro Rc Ri 295K Rc << Ro, Ri

  13. Ro Example 2 Rc Ri 305K? 295K Rc << Ro, Ri =(295+305)/2

  14. =373-(373-300)*[98.1/(98.1+11400)] =372.3K

  15. Example 3

  16. Forced Convection For External Flow Flow Parallel To Plane Surface

  17. Cylinders In Crossflow

  18. Tube Banks In Crossflow SL : Center-to-center distance between tubes along the direction of flow ST: Center-to-center distance between tubes normal to the direction of flow

  19. Adapted from ID Page 437

More Related