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Three-dimensional mixed convection flow with variable thermal conductivity and frictional heating
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M Qasim,N Riaz,Dianchen Lu,S Shafie
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Table 1. Effects of different physical parameters on ${F}^{{\prime\prime} }\left(0\right),-{G}^{{\prime\prime} }\left(0\right),$ ${{\rm{\Theta }}}^{{\prime\prime} }\left(0\right)$ and comparison between shooting method and built-in routine bvp4c in Matlab.
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| | | | | $-{F}^{{\prime\prime} }\left(0\right)$ | $-{G}^{{\prime\prime} }\left(0\right)$ | $-{{\rm{\Theta }}}^{{\prime} }\left(0\right)$ |
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λ | ${\Pr }$ | Ec | δ | ϵ | Shooting | bvp4c | Shooting | bvp4c | Shooting | bvp4c |
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0.0 | 1.2 | 0.6 | 0.2 | 0.5 | 1.569 89 | 1.569 62 | 0.784 94 | 0.784 75 | 1.823 65 | 1.823 55 | 0.5 | 1.2 | 0.6 | 0.2 | 0.5 | 1.271 68 | 1.271 24 | 0.806 53 | 0.806 12 | 1.932 93 | 1.932 77 | 1.0 | 1.2 | 0.6 | 0.2 | 0.5 | 0.996 57 | 0.996 18 | 0.823 76 | 0.823 45 | 2.015 22 | 2.015 09 | 1.5 | 1.2 | 0.6 | 0.2 | 0.5 | 0.735 65 | 0.735 44 | 0.838 61 | 0.838 36 | 2.080 27 | 2.080 11 | 1.2 | 0.3 | 0.6 | 0.2 | 0.5 | 0.591 71 | 0.591 49 | 0.865 19 | 0.864 87 | 1.007 37 | 1.007 23 | 1.2 | 0.7 | 0.6 | 0.2 | 0.5 | 0.773 96 | 0.773 64 | 0.843 76 | 0.843 42 | 1.556 59 | 1.556 41 | 1.2 | 1.2 | 0.6 | 0.2 | 0.5 | 0.890 79 | 0.890 47 | 0.829 93 | 0.829 78 | 2.042 99 | 2.042 81 | 1.2 | 6.7 | 0.6 | 0.2 | 0.5 | 1.171 19 | 1.170 98 | 0.803 08 | 0.802 73 | 4.752 33 | 4.752 02 | 1.2 | 1.0 | 0.0 | 0.2 | 0.5 | 0.892 27 | 0.892 06 | 0.829 71 | 0.829 65 | 2.033 36 | 2.033 22 | 1.2 | 1.0 | 1.0 | 0.2 | 0.5 | 0.827 28 | 0.826 95 | 0.837 35 | 0.837 19 | 1.760 31 | 1.760 17 | 1.2 | 1.0 | 2.0 | 0.2 | 0.5 | 0.771 27 | 0.771 13 | 0.843 79 | 0.843 52 | 1.524 76 | 1.524 61 | 1.2 | 1.0 | 3.0 | 0.2 | 0.5 | 0.722 07 | 0.721 95 | 0.849 35 | 0.849 14 | 1.316 99 | 1.316 71 | 1.2 | 1.0 | 0.5 | 0.0 | 0.5 | 0.887 74 | 0.887 55 | 0.830 98 | 0.830 65 | 2.129 88 | 2.129 69 | 1.2 | 1.0 | 0.5 | 1.0 | 0.5 | 0.765 63 | 0.765 48 | 0.843 08 | 0.842 88 | 1.375 84 | 1.375 77 | 1.2 | 1.0 | 0.5 | 2.0 | 0.5 | 0.683 16 | 0.683 03 | 0.852 15 | 0.851 94 | 1.081 84 | 1.081 69 | 1.2 | 1.0 | 0.5 | 3.0 | 0.5 | 0.622 25 | 0.622 11 | 0.859 14 | 0.858 92 | 0.916 69 | 0.916 52 |
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