Convection and Conduction Heat Transfer Part 1 pdf

... Convection and Conduction Heat Transfer, Edited by Amimul Ahsan p. cm. ISBN 978-953-307-582-2 Convection and Conduction Heat Transfer 18 Gr = 10 5 11 010 0 Nu 4 5 6 7 8 9 10 11 12 γ ... Conduction Heat Transfer 12 Re =1. 0; Re=5.0; Re =10 .0; Gr =10 3 4 Gr =10 5 Gr =10 Re =1. 0; Re=5.0; Re =10 .0; Re =1. 0; Re=5.0; Re =10 .0; Gr =10 5 4 Gr...

Ngày tải lên: 21/06/2014, 01:20

... Convection and Conduction Heat Transfer 12 Re =1. 0; Re=5.0; Re =10 .0; Gr =10 3 4 Gr =10 5 Gr =10 Re =1. 0; Re=5.0; Re =10 .0; Re =1. 0; Re=5.0; Re =10 .0; Gr =10 5 4 Gr =10 3 Gr =10 Gr =10 5 4 Gr =10 3 Gr =10 1 5 ° 0° 90° 7 5 ° 45° 3 0 ° 6 0 ° 1 5 ° 0° 90° 7 5 ° 45° 3 0 ° 6 0 ° 1 5 ° 0° 90° 7 5 ° 45° 3 0 ° 6 0 ° 1 5 ° 0° 90° 7 5 ° 4 5 ° 3 0 ° 6 0 ° 1 5 ° 0° 9...

Ngày tải lên: 19/06/2014, 10:20

... References Convection and Conduction Heat Transfer 72 R i = 1 R i = 1 R i = 1 R i = 1 Fig. 12 . Contours of streamlines and isotherms at Re=400, A =1. 5 and Ф=30°, opposing flow 18 ... Convection and Conduction Heat Transfer 68 R i = 0 .1 R i = 1 R i = 5 R i = 10 Fig. 7. Contours of streamlines and isotherms at R...

Ngày tải lên: 19/06/2014, 10:20

... cooling, J .Heat Transfer 11 0 (19 88) 10 97 11 11. [5] C. K. Cha and Y. Jaluria, Recirculating mixed convection flow for energy extraction, Int. j. Heat Mass Transfer 27 .18 01- 1 810 11 984). [6] ... (figure 11 .b.). z/R Nu 0 5 10 15 20 5 10 15 20 25 30 _ _ _ Legend: Galerkin Collocation z/R Nu 0 5 10 15 20 5 10 15 20 25 30 Legend: Galerkin Collocation 0 (a)...

Ngày tải lên: 19/06/2014, 10:20

... 2.523 10 2.220 0.000 2.220 0.000 2.220 50 1. 118 0.000 1. 118 0.000 1. 118 Without 10 0 1. 116 0.000 1. 116 0.000 1. 116 0 4.049 36.733 2 .10 5 38.678 40.783 10 3.754 36.759 1. 874 38.6 41 40. 513 50 ... medium: () 1 2, 1, m 1 r 1, 1, 1, 0r 1, where 1 [1 273 ,15 ] nn kk n kk n k k TGT x TG G T α λγ β + + + Δ == + +− , ( 51) () 1 p ,2 ,1 m 1 ,1 ,1 ,1...

Ngày tải lên: 19/06/2014, 10:20

... 10 00 0 2 4 6 8 10 12 14 d =1 d=2 d=3 Gr =10 3 - Heater 2 1 10 10 0 10 00 Nu 0 2 4 6 8 10 12 d =1 d=2 d=3 Gr =10 4 - Heater 1 1 10 10 0 10 00 0 2 4 6 8 10 12 14 d =1 d=2 d=3 Gr =10 4 - Heater 2 1 10 10 0 ... 0° Re 10 0 10 1 10 2 10 3 NU 0 2 4 6 8 10 12 14 16 NUH1 NUH2 NUH3 Gr =10 4 , γ = 45° Re 10 0 10 1 10 2 10 3 NU 0 2 4 6 8 10 12 14 1...

Ngày tải lên: 19/06/2014, 10:20

... 0. 813 1. 117 (c) 3.566 3.544 1. 165 (d) 3.9 91 0 .17 0 3.9 31 0.825 1. 1 01 1.298 16 77 3.699 0 .17 7 3.653 0. 812 1. 098 1. 194 6557 3 10 3.695 0 .17 9 3.645 0.820 1. 089 1. 196 10 197 4 10 19 . 51 0 .12 0 16 .24 ... 0 .1 1e-04 17 .562 37.055 3.0 71 4.607 40397 0 .1 1e-05 2 10 1 17 .603 36.873 3.086 4.655 16 0797 0 .1 1e-05 13 .42 (b) 72.560 4 41. 7...

Ngày tải lên: 19/06/2014, 10:20

... 2.0440888 412 9753 91 50 0.7775905 213 06 015 2 0.465292587 011 5464 1. 5787962542859926 2.0440888 412 9753 91 100 0.7775905 213 06 015 2 0.465292587 011 5464 1. 5787962542859926 2.0440888 412 9753 91 200 0.7775905 213 06 015 2 ... + 1 2 − 1  L + 1 −  L + 1 +   β  1 0 ≤  ≤ L and β 0 = 1 188 Convection and Conduction Heat Transfer 14 Will-be-set-by-IN-TECH...

Ngày tải lên: 19/06/2014, 10:20

... 8A 5 0 .1 0 .1 2.0 Min 1, 0 Fig 8B 5 0 .1 0 .1 2.0 Max 1, 61 Fig 8C 5 0 .1 0 .1 2.0 1. 5 1. 5 Fig 8D 6 0 .1 2.0 0 .1 0 .15 0 .15 Fig 8E 6 0 .1 2.0 0 .1 Min 0 .13 Fig 8F 6 0 .1 2.0 0 .1 Max 0 .19 Table ... 2.0 2.0 2,0 2 0 .15 10 Fig 9D 5 4 0.075 0 .1 0 .1 1.85 1. 85 1 0 .15 10 Fig 9E 5 4 0.075 0 .1 0 .1 Min 1. 65 1 0 .15 10 Fig 9F 5 4 0.075 20...

Ngày tải lên: 19/06/2014, 10:20

... = a/R; 2 X1 ;=+δ 1 11 1 Hln1K1; 2K K ⎛⎞ π =−+ ⎜⎟ ⎝⎠ 2 1 1 K1 . λ =− λ The correction factor ϕ sc is given by 22 2 cc 11 sc 22 22 2 2 1 1 c 1 22 rr 1K 11 ln 2K 2R R K r 1K 1 R ⎡ ⎤ ⎢ ⎥ ⎛⎞ πλ ... given by the following equations: at δ ≤ 1 () () () 2 ad 211 1 4 1 1 11 1 H arcsin X 1 1 ln 2KK1K K 4arcsin /X 11 1ln 11 XK X 21 ⎡ ⎛⎞ λ πδ π = −−δ+δ δ+ −δ− − ⎢...

Ngày tải lên: 19/06/2014, 10:20