Heat Transfer Engineering Applications Part 1 potx

... Klaumünzer, S. (19 95). Model of track formation, Physical Review B 51( 18): 12 107 12 115 . URL: http://link.aps.org/doi /10 .11 03/PhysRevB. 51. 1 210 7 Sands, D. (2 011 ). Pulsed laser heating and melting, ... shaped embedded Au nanoparticles, Applied Physics Letters 94 (11 ): 11 310 7. URL: http://link.aip.org/link/APPLAB/v94/i 11/ p 113 107/s1&Agg=doi 83 Energy Transfer in Ion– a...

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... Yz       , j = 1, , M -1; (42) 11 ,,2, ,1 111 1 tt t tt tt f w jf w jf w jf w j SU TT T Zt Z Zz        , j = 2, , M. (43) In the above equations: 11 1 11 11 1 11 11 1 1 ,,, , VBCV ...      , j = 1, , M; (40) 11 1 , ,1, 2, ,1 111 1 1 tt t tt tt tt c gj c gj c gj c gj c gj KL P TT T Xt X X Xz         , j = 2, , M;...

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... 0 30z  m, 0 15 z  m, 0 0z  m, respectively. (a) 0 30z  m (b) 0 15 z  m (c) 0 0z  m 10 m10 m10 m 10 m10 m10 m 10 m10 m10 m 10 m10 m10 m 10 m10 m10 m 10 m10 m10 m ... follows: 1. For 1 1 j         22 2 2 2 11 ,1 11, 1 , 222 11 1 j ii i jj ii j ij jii rrI rI I rr            , max 1, 2, ,ii  (5) 0,...

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... be investigated. 73 Energy Transfer in Ion– and Laser–Solid Interactions Pulsed Laser Heating and Melting 53 2 1 2 1 2 0 11 () 22 11 22 1 2( ) 2( ) (1 ) (,) 1 [( ) ] [( ) ] 2 () () z Dt zz z Dt ... distance r from the ion’s path after 10 12 s according to D’Orléans et al. (2003). 74 Heat Transfer - Engineering Applications Heat Transfer – Engineering...

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... ±<T 0 /T 1 >/90± <T 0 /T 1 >] S leads to a minimum temperature at the plate center at [T 0 =75º, T 1 =0º]. 0.8 0.9 1 1 .1 1.2 1. 3 1. 4 1. 5 0.7 0.8 0.9 1 1 .1 1.2 1. 3 1. 4 1. 5 1. 6 1. 7 Fig. ...     011 22 kKKVKV (9)                   11 22 11 22 01 11 22 11 22 22 11 2 22 11 0.5 0 0.5 0 00....

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... 3 .15 9 10 13 1. 466 10 4 5.492 10 8 9.973 3 k 2 .18 2 10 7 8.4 01 10 3 1. 880 10 9 9.965 4 k 1. 089 10 7 8.438 10 3 1. 160 10 9 9.863 5 k 1. 523 10 9 1. 119 10 4 1. 2 81 10 9 1. 135 10 Table ... of 10 K (Onishi and Fukutani, 2003a). Sulfur concentration 1 wt % 5 wt % A i (1/ s) E i /R (K) A i (1/ s) E i /R (K) 1 k 1. 034 10 7 1....

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...                       2 22 22 22 2 2 22 (1) cosh 11 21 11 11 11 1 1 1 21 61 1 1cosh DC s s Cs Cs sC DC C s DC DC C s DC t D D C s s CDC Cs DC s        ... Nu conv Gr * Pr Painted(E=0.96) Unpainted(E=0.78) -10 0 10 20 30 40 50 60 70 80 90 10 0 40 50 60 70 80 90 10 0 11 0 12 0 13 0 Nu conv Nu av Nu  /  /L=0 .1...

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... 1. 0 0.0 1. 0x10 -4 2.0x10 -4 3.0x10 -4 4.0x10 -4 5.0x10 -4 6.0x10 -4 (m) x ( m ) =0.80 =0.85 =0.90 =0.95 0.0 0.2 0.4 0.6 0.8 1. 0 0.0 2.0x10 -4 4.0x10 -4 6.0x10 -4 8.0x10 -4 1. 0x10 -3 1. 2x10 -3 1. 4x10 -3 1. 6x10 -3 (m) x(m) ... condensation heat transfer coefficient. 0.00.20.40.60. 81. 0 0.0 1. 0x10 -4 2.0x10 -4 3.0x10 -4 4.0x10 -4 5.0x10 -4 (m) x ( m ) Ja...

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... temperature with depth Heat Transfer – Engineering Applications 238         1, 1, 11 11 11 1/ 2, 1, , 1/ 2, , 1, , 22 11 11 1 1/2, , 1 , 1/ 2, , , 1 ,, p 2 2 , 2 ij ij nn nn nn i j ... follows: 1 2.35r  , Heat Transfer – Engineering Applications 248 50 10 0 15 0 200 250 300 6.0x10 -7 7.0x10 -7 8.0x10 -7 9.0x10 -7 1. 0x10...

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