3  elsevier  expert systems with applications an international journal 2014

... Investig(al)sT Inaanismkad7ahB1erTand 167 Heat Transfer Engineering, 31 (3) :168–178, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 630 9 033 0 434 3 Performance ... vol 31 no 2010 Heat Transfer Engineering, 31 (3) :179–192, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 630 9 033 0 435 0 Heat Transfer and ... heating and cooling vol 31 no 2010 Heat Transfer Engineering, 31 (3) :1 93 200, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 630 9 033 0 436 8...

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... YOUNG ET AL 2 23 390 600 38 8 o 550 0. 93 C / hr o 1 .32 C / hr 500 38 4 450 o 0.88 C / hr 38 2 o 0.9 C / hr 38 0 400 o 0. 73 C / hr 35 0 37 8 o 0.92 C / hr 30 0 37 6 250 37 4 Figure 11 EDS analysis of a deposit ... crude oil [24] 50 100rpm 0.012 225 200rpm 30 0rpm ln A (m K / kJ) 40 30 0.008 20 10 0.004 0 50 100 150 200 250 30 0 -10 -20 31 0 32 0 33 0 34 0 35 0 36 0 37 0 38 0 39 0 400 EA (kJ/mol) o Surface Temperature, ... heat exchangers vol 32 nos 3 4 2011 Heat Transfer Engineering, 32 (3 4):228– 236 , 2011 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 632 .2010.495606...

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... 1.0100 1 .36 1 1 .39 18 0 .32 56 0 .33 5 3. 1141 3. 2090 3. 236 0 16.9 134 17.2800 17.9400 35 .8766 36 . 530 0 35 .9240 53. 1089 53. 4200 — 64 .37 45 102.2627 0 .38 8 0 .36 770 3. 777 3. 58548 22. 53 88.65◦ 90◦ 80.55◦ 81◦ 81◦ ... Flux Model, International Journal of Heat and Mass Transfer, vol 36 , pp 36 03 36 24, 19 93 [16] Anderson, D A., Tannehill, J C., and Pletcher, R H., Computational Fluid Mechanics and Heat Transfer, ... 2.27E -3 0.08E -3 5.17E-2 3. 68E-2 0.712 2.62E-4 540 2.67E -3 0.10E -3 5.28E-2 3. 89E-2 0. 736 4 .35 E-4 540 2.81E -3 0.10E -3 5.79E-2 4.29E-2 0.741 6.86E-4 1100 1.45E -3 0.10E -3 3.88E-2 2.01E-2 0.519 5.61E-3...

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... 1.52 Nu [4] 3. 414 2.946 5.785 4.991 9.802 8.457 16.608 14 .32 8 Nu (present study) 3. 374 2.9 23 5. 639 4.884 9.4 23 8.161 15.747 13. 638 Difference (%) 1.17 0.78 2.52 2.14 3. 87 3. 50 5.18 4.82 and 100 cm ... transfer physics vol 31 no 2010 Heat Transfer Engineering, 31 (2):108–118, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 630 9 032 8 536 9 ... Engineering, 31 (2):127– 137 , 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 630 9 032 8 538 5 Electrohydrodynamic Induced Flow and Heat Transfer...

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... Boiling Heat Transfer of Freon R11 and HCFC1 23 in Narrow Passages, International Journal of Heat and Mass Transfer, vol 43, pp 33 47– 33 58, 2000 [21] Yu, W., France, D M., Wambsganss, M W., and Hull, ... Nanofluidics, doi: 10.1007/s10404-008- 034 8-7, 2008 [ 13] Tran, T N., Wambsganss, M W., and France, D M., Small Circular- and Rectangular-Channel Boiling with Two Refrigerants, International Journal ... Physics, vol 230 , pp 2 53 265, 1998 [ 43] Yan, Y Y., and Lin, T F, Evaporation Heat Transfer and Pressure Drop of Refrigerant R- 134 a in a Small Pipe, International Journal of Heat and Mass Transfer,...

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... × 130 3. 7007 3. 6052 3. 5 830 3. 5762 3. 5 739 3. 5 730 3. 9877 3. 9566 3. 9496 3. 9476 3. 9469 3. 9469 4.2704 4. 132 3 4.1145 4.1105 4.10 93 4.1092 2.65 0.62 0.19 0.06 0.02 — 0.79 0.18 0.05 0.02 0.00 — 3. 34 ... 1541. 732 079 − 43. 238 990 − 939 .27 930 4 −0.1 232 63 189. 432 570 19 .35 9815 1.417 233 E-02 −12.690997 −2.0 535 67 3. 604 831 E-02 Therefore, heat is transferred mainly by conduction in these zones Heat Transfer ... microchannels Height (µm), h ± 100 200 30 0 400 500 710 Length (mm), l± 0.05 w ± 0.05 Width (mm), w/ h Shorter, ls Longer, ll 37 37 37 37 37 47 37 0.0 185.0 1 23. 3 92.5 74.0 66.2 30 30 30 30 30 40...

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... 53. 63 52 .38 52.61 53. 11 52.01 53. 10 52.65 53. 13 3197.71 37 97.45 36 37.99 39 45.14 4925 .37 4149 .39 4744.86 4 936 .54 4856.12 631 3.95 4910.87 5966.89 632 3.06 6085.50 532 6.84 7405.08 7484.57 7972 .32 ... 56. 63 56.61 56 .33 55.17 57.16 56.72 56.27 57.26 57 .38 56. 43 56 .34 1 131 7.56 7810. 43 8888.05 133 63. 95 6598.56 131 14.69 932 3.26 70 03. 86 8519 .38 130 56.92 14820. 23 7000.42 10104.50 15291.82 79 43. 11 ... 151210 1 532 30 155690 15 632 0 158950 1 635 30 1 632 60 164850 165170 164060 165210 16 632 0 168210 168950 17 032 0 17 135 0 17 235 0 1 738 60 17 435 0 1 733 40 17 435 0 175950 174240 175270 176420 177010 177150 177 630 178240...

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... Model, International Journal of Heat and Mass Transfer, vol 43, pp 16 03 1616, 2000 [155] Jang, Y J., Chen, H C., and Han, J C., Computation of Flow and Heat Transfer in Two-Pass Channels With 60 ... ASME Journal of Heat Transfer, vol 1 23, pp 5 63 575, 2001 [156] Jang, Y J., Chen, H C., and Han, J C., Numerical Prediction of Flow and Heat Transfer in a Two-Pass Channel With 90 Deg Ribs, International ... Flow and Heat Transfer in a Smooth and Ribbed U-Duct With and Without Rotation, ASME Journal of Heat Transfer, vol 1 23, pp 219– 232 , 2001 [160] Suga, K., Predicting Turbulence and Heat Transfer...

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... 0.268 0 .36 4 0.414 0.466 0.577 0.700 0. 839 5 .31 8 4.201 3. 849 3. 7 03 3.6 63 3.642 3. 618 3. 610 3. 609 3. 608 5.547 4.511 4.018 3. 721 3. 615 3. 528 3. 398 3. 314 3. 511 3. 489 4. 13 6.87 4.19 0.49 −1 .33 3. 26 ... −6.48 −8. 93 −2.78 3. 41 10 20 ∞ 3. 546 3. 608 3. 678 3. 724 3. 766 3. 780 3. 797 3. 809 3. 852 3. 867 3. 368 3. 726 3. 809 3. 872 3. 915 3. 945 3. 966 3. 982 4. 033 4.051 heat transfer engineering vol 31 no 2010 ... 19 83 [2] Wang, G., and Vanka, S P., Convective Heat Transfer in Periodic Wavy Passages, International Journal of Heat and Mass Transfer, vol 38 , no 17, pp 32 19 32 30, 1995 [3] Niceno, B., and...

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... points within ±5% ±10% ±15% 1065 (37 .4%) 1597 (56.1%) 1082 (38 .0%) 1244 ( 43. 7%) 16 43 (57.8%) 136 9 (48.1%) 1718 (60.4%) 2 137 (75.1%) 2 139 (75.2%) 2059 (72.4%) 20 03 (70.4%) 2084 ( 73. 3%) 19 53 (68.6%) ... mini and microtubes and two-phase flow heat transfer vol 31 no 2010 Heat Transfer Engineering, 31 (9): 733 –741, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online ... ±20% within ±25% within 30 % Average deviation range (%) Range of parameters ReSL ReSG PrG /PrL µG /µL 10 3 33. 1 649 (66%) 746 (76%) 817 ( 83% ) 20.5 111 ( 63% ) 140 (80%) 154 (88%) −16.9 to 30 .8...

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... Effects of Enhanced Surfaces and Surface Orientations on Nucleate and Film Boiling Heat Transfer in R-11, International Journal of Heat and Mass Transfer, vol 30 , pp 2627–2 639 , 1987 [3] Kang, M G., ... Oil Nus = 0.0 533 Re0.688 Pr1 /3 s −0.45 fs = 1.64Res Nus = 0. 032 3Re0.742 Pr1 /3 s −0 .33 fs = 0.63Res 1 /3 Nus = 0.026Re0.8 s Pr Oil 0.4 Nus = 0. 030 Re0.8 s Pr Oil Nus Nus Nus Nus Nus Wang et al [48] ... namely, R- 134 a and mixtures of R- 23 and R- 134 a, with the concentration of R- 23 varying from up to 11% The finned tubes had 433 , 748, 1,024, 1,260, and 1,574 fins per meter The enhanced tube tested...

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... 40 60 30 55 50 20 45 40 2 73 K 2 83 K 2 93 K 30 3 K 31 3 K 32 3 K 32 8 K 33 3 K Enthalpy (J/mol) 50 Internal energy (J/mol) 75 70 0.4 0.6 0.8 30 3 K xdes/xm 32 3 K 33 3 K C 34 3 K 35 3 K 36 3 K B 1.2 1. 03 bar ... 2 73 K 31 3 K 34 3 K 45 2 93 K 32 3 K 35 3 K 30 3 K 33 3 K 36 3 K 40 0.2 0.4 0.6 0.8 x/xm Figure Enthalpy versus concentration for Maxsorb III + R 134 a as a function of pressure and temperature heat transfer ... performance: Cooling power COP Without auxiliary heater With auxiliary heater 80◦ C 33 ◦ C 33 ◦ C 20◦ C 1.44 m3 /h 1.44 m3 /h 0 .30 m3 /h 0 .30 m3 /h 90◦ C 33 ◦ C 33 ◦ C 20◦ C 1.44 m3 /h 1.44 m3 /h 0 .30 ...

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... Heat Transfer Engineering, 31 (12):9 63 964, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 631 0 036 389 03 editorial Advances in Heat Transfer ... heat exchangers vol 31 no 12 2010 Heat Transfer Engineering, 31 (12):9 73 980, 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 631 0 036 38952 ... no 3, pp 35 1 35 8, 1986 Haynes, B S., and Fletcher, D F., Subcooled Flow Boiling Heat Transfer in Narrow Passages, International Journal of Heat Mass Transfer, vol 46, no 19, pp 36 73 36 82, 2003...

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... Heat Transfer Engineering, 31 ( 13) :10 23 1 033 , 2010 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 631 0 036 39059 Two-Phase Flow ... engineer and a member of the American Institute for Aeronautics and Astronautics (AIAA) and the American Society of Mechanical Engineers (ASME) vol 31 no 13 2010 Heat Transfer Engineering, 31 ( 13) :1 034 –1041, ... Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 631 0 036 39075 U-Tube Assembly Heat Exchanger Performance Analysis Using Cyclic Iteration COREY CANTRELL and...

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... · · · + θn−1 n=0 heat transfer engineering 2Rb ln Rb m 2m Rb 2m 2m √ I −I−2 /3 3√ 3 Rb −2 /3 Rb 2m R 2m 2m b I−2 /3 3√ R I−1 /3 −I2 /3 3√ R b b I2 /3 2m Rb 2m Rb I1 /3 I2 /3 (31 ) where Iν is the first ... boards of the International Journal of Heat and Mass Transfer and International Communications in Heat and Mass Transfer, International Journal of Thermal Sciences, International Journal of Numerical ... S., and Eastman, J A., Mechanisms of Heat Flow in Suspensions of NanoSized Particles (Nanofluids), International Journal of Heat and Mass Transfer, vol 45, pp 855–8 63, 2002 [ 23] Louge, M., and...

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... in Fin-and-Tube Heat Exchanger Applications, International Journal of Heat and Mass Transfer, vol 45, pp 38 03 38 15, 2002 [20] Torii, K., Kwak, K M., and Kishino, K., Heat Transfer Enhancement ... Temperature and Flow, International Journal of Heat and Mass Transfer, vol 49, pp 10 83 1089, 2006 [10] Tandiroglu, A., and Ayhan, T., Energy Dissipation Analysis of Transient Heat Transfer for ... a Rectangular Channel With a Vee-Shaped Vortex Generator, International Journal of Heat and Fluid Flow, vol 28, pp 30 6 31 7, 2007 [14] Leu, J S., Wu, Y H., and Jang, J Y., Heat Transfer and Fluid...

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... transfer engineering vol 32 no 2011 Heat Transfer Engineering, 32 (2): 133 –140, 2011 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 online DOI: 10.1080/01457 631 0 037 69211 ... 55, pp 30 42 30 64, 1988 heat transfer engineering [18] Bendat, J S., and Piersol, A G., Random Data Analysis and Measurement Procedures, 3rd ed., John Wiley and Sons, New York, pp 37 4 37 6, 2000 ... in a Standard Flammability Channel Using PIV, Proc XII Symp Heat Mass Transfer, Cracow, Poland, pp 33 1 33 8, 2004 Fodemski, T R., and Gorecki, G., Experimental and PIVMethod Studies of Lean Mixture...

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... refrigerants in conventional channels and in mini-channels vol 32 no 2011 Heat Transfer Engineering, 32 (5) :36 9 38 3, 2011 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 print / 1521-0 537 ... 0), so Eqs (27) and (30 ) and Eqs (28) and (31 ) become, respectively, NTU = ε= 1 − Rε ln 1− R 1−ε exp [N T U (1 − R)] − exp [N T U (1 − R)] − R (32 ) (33 ) Equations (32 ) and (33 ) are the same as ... heat transfer in two-phase systems, and nuclear reactor thermal hydraulics vol 32 no 2011 Heat Transfer Engineering, 32 (5) :38 4 38 9, 2011 Copyright C Taylor and Francis Group, LLC ISSN: 0145-7 632 ...

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... 0.0 0 .3 0.8 0.8 0 .3 0 .3 0.8 0.8 0 .3 0 .3 0.8 0.8 0 .3 0 .3 0.8 0.8 0 .3 0. 03 0. 03 0 .3 0 .3 0. 03 0. 03 0 .3 0 .3 0. 03 0. 03 0 .3 0 .3 0. 03 0. 03 0 .3 0 .3 (0.0111, 0.4777) (0.0097, 0.5175) (0.0107, 0.57 03) (0.0092, ... vol 32 no 2011 466 [28] [29] [30 ] [31 ] [32 ] [33 ] [34 ] [35 ] [36 ] [37 ] [38 ] R DAS ET AL Heat Flux, International Journal of Heat and Mass Transfer, vol 30 , pp 16 23 1 631 , 1987 Chu, H S., Lin, S., and ... in Convergent Channels, International Journal of Heat and Mass Transfer, vol 53, pp 35 13 35 24, 2010 [15] Bianco, N., Langellotto, L., Manca, O., and Nardini, S., Thermal Design and Optimization...

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... 20 30 30 30 30 20 20 20 20 20 20 25 25 25 25 25 25 13. 3 13. 3 13. 3 13. 3 13. 3 13. 3 20 20 20 20 20 20 20 20 20 20 20 20 0 0 90 90 0 90 90 0 90 90 90 0 90 90 90 0 90 90 90 45 45 45 135 135 135 23 ... 30 15 40 50 30 23 40 50 30 40 50 4.48 6.2 7.79 4.06 5.85 7.55 3. 82 5 .33 7 .3 0. 23 0.17 0.16 0.25 0.178 0.16 0.265 0.196 0.16 0.6 83 0.726 0.772 0.674 0.722 0.774 0.654 0.708 0.782 23. 8 23. 85 23. 5 ... [50] [51] [52] [ 53] [54] [55] [56] [57] 539 tion of the Model, International Journal of Heat and Mass Transfer, vol 47, pp 33 75 33 85, 2004 Jacobi, A M., and Thome, J R., Heat Transfer Model for...

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