Convection and Conduction Heat Transfer Part 5 ppt
Convection and Conduction Heat Transfer Part 5 ppt
... 19. 658 160797 1 1e- 05 257 .394 4946.968 36.720 35. 436 10197 1 5e- 05 287.3 75 4880.108 44.2 95 49.2 35 40397 5 5e-06 4 10 1 287.3 75 4880.197 44.2 95 49.310 160797 5 1e-06 2.1 35 2.148 (a) 50 ... 211.67 61 .55 15. 91 (d) 1 95. 98 0.0 45 63.73 0. 850 6.1 15. 15 1677 219.48 0.038 64.87 0. 851 7.67 16.13 655 7 221.37 0.039 65. 91 0.860 8.97 16 .51 10197 7 10 68...
Ngày tải lên: 21/06/2014, 01:20
Convection and Conduction Heat Transfer Part 2 ppt
... 2 t 51 0 152 0 NU 5 10 15 20 25 30 Heater 1 Heater 2 Re = 1000, d = 2 t 51 0 152 0 NU 5 10 15 20 25 30 Heater 1 Heater 2 Re = 10, d = 3 t 51 0 152 0 NU 5 10 15 20 25 30 Heater 1 Heater 2 Re = 100, d = 3 t 51 0 152 0 NU 5 10 15 20 25 30 Hea ... 1 t 2468101214 NU 5 10 15 20 25 30 Heater 1 Heater 2 Re = 1000, d = 1 t 2468101214 NU 5 10 15 20 25 30 Heater 1...
Ngày tải lên: 19/06/2014, 10:20
Convection and Conduction Heat Transfer Part 5 doc
... 3 154 1e-4 15 3 259 5e- 05 51 3706 8.44e-6 5 10 10e-2 1e-te04 5 159 0 1e-4 14 1244 5e- 05 43 4090 1.06e -5 6 10 1 1e-04 4 55 27 1e-4 14 56 08 1e- 05 283 144089 1.38e-4 7 10 5 1e- 05 6 18 250 1e -5 ... 19. 658 160797 1 1e- 05 257 .394 4946.968 36.720 35. 436 10197 1 5e- 05 287.3 75 4880.108 44.2 95 49.2 35 40397 5 5e-06 4 10 1 287.3 75 4880.197 44.2 95 49.3...
Ngày tải lên: 19/06/2014, 10:20
Convection and Conduction Heat Transfer Part 7 ppt
... 0.4 652 9 258 37970406 1 .57 8796021 957 4921 2.0440886 057 5 453 27 100 0.77 759 0426 152 655 1 0.4 652 9 258 37970406 1 .57 8796021 957 4921 2.0440886 057 5 453 27 150 0.77 759 0426 152 655 1 0.4 652 9 258 37970406 1 .57 8796021 957 4921 ... 0.4 652 9 258 17800941 1 .57 87 958 7 158 591 25 2.044088 453 3660064 150 0.77 759 03643992 450 0.4 652 9 258 17800941 1 .57 87 958 7 158 591 25 2....
Ngày tải lên: 19/06/2014, 10:20
Convection and Conduction Heat Transfer Part 10 pptx
... hys 64 :55 1 56 1. Convection and Conduction Heat Transfer 266 By the use of the divergent theorem, [ ] ( ) ˆ ii jj i kTd kT nd qnd ΩΓΓ − ∇• ∇ Ω=− ∇ • Γ= Γ ∫∫∫ (20) where the heat flux ... the thermal properties and source term. Taking k ( T ) = T c v ( T ) = 1 ( 25) s ( x, t ) = − 3 − ( 6 + λr ) e −λt − 3e −2λt 288 Convection and Conduction Heat Transfer...
Ngày tải lên: 19/06/2014, 10:20
Convection and Conduction Heat Transfer Part 14 pptx
... 423 K 150 W/m 2 K C 1 -1 -1 -1 806.799 2 -1 -1 0 7 75. 9 45 3 -1 -1 +1 862.902 4 -1 0 -1 800.301 5 -1 0 0 769.408 6 -1 0 +1 855 . 752 7 -1 +1 -1 798.197 8 -1 +1 0 767 .56 2 9 -1 +1 +1 854 .967 ... This Convection and Conduction Heat Transfer 384 The initial and boundary conditions were applied to geometry of Figure 1 according to Table 1. The boundary conditi...
Ngày tải lên: 19/06/2014, 10:20
Convection and Conduction Heat Transfer Part 14 ppt
... 423 K 150 W/m 2 K C 1 -1 -1 -1 806.799 2 -1 -1 0 7 75. 9 45 3 -1 -1 +1 862.902 4 -1 0 -1 800.301 5 -1 0 0 769.408 6 -1 0 +1 855 . 752 7 -1 +1 -1 798.197 8 -1 +1 0 767 .56 2 9 -1 +1 +1 854 .967 ... & Lalovic, 20 05) : ( ) + ( ) (1 ( ) ( ) ( ) (1 2/) (5) Convection and Conduction Heat Transfer 384...
Ngày tải lên: 21/06/2014, 01:20
Convection and Conduction Heat Transfer Part 11 ppt
... Datasets 12 Heat Transfer Book 2 0 0 .5 1 1 .5 2 - 15 -5 5 15 Thermal Conductivity (W/ m. K Temperature (Celcius) (a) Variation of k 0 20 40 60 80 100 - 15 -5 5 15 Specific heat Capacity (KJ / Kg.K Temperature ... cases involving irregular datasets and rapid variations in governing properties will tend to favour 292 Convection and Conduction Heat Transfer Convection...
Ngày tải lên: 21/06/2014, 01:20
Convection and Conduction Heat Transfer Part 1 doc
... 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° 90° 7 5 ° 4 5 ° 3 0 ° 6 0 ° 1 5 ° 0° 90° 7 5 ° 4 5 ° 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...
Ngày tải lên: 19/06/2014, 10:20
Convection and Conduction Heat Transfer Part 3 pdf
... 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 Re=400, A=1.0 and γ=60° Convection and Conduction ... Will-be-set-by-IN-TECH Convection and Conduction Heat Transfer 70 R i = 0.1 R i = 1 R i = 5 R i = 10 Fig. 10. Contours of streamlines an...
Ngày tải lên: 19/06/2014, 10:20