Table 3 Comparison of non-dimensionless physical variable effect against surface drag coefficient and convective heat transfer.
\(\alpha \) | \(R\) | \(M\) | \({\varphi }_{1}\) | \({\varphi }_{2}\) | \({n}_{1}\) | \({n}_{2}\) | \(Pr\) | \({\left|{C}_{f}\right|}_{\eta =-1}\) | \({\left|{Nu}_{z}\right|}_{\eta =-1}\) |
---|---|---|---|---|---|---|---|---|---|
0.1 | 0.01 | 1 | 0.01 | 0.01 | 3 | 3 | 6.2 | 3.1080 | 0.4302 |
0.2 | \(3.0262\) | \(0.3508\) | |||||||
0.3 | \(2.9437\) | \(0.2842\) | |||||||
0.4 | \(2.8623\) | \(0.2288\) | |||||||
− 0.02 | \(3.0801\) | \(0.3362\) | |||||||
− 0.03 | \(3.0591\) | \(0.2738\) | |||||||
− 0.04 | \(3.0485\) | \(0.2464\) | |||||||
− 1 | \(\begin{array}{c}2.723\end{array}1\) | \(0.4304\) | |||||||
− 2 | \(\begin{array}{c}2.5132\end{array}\) | \(0.4305\) | |||||||
− 3 | \(2.2893\) | \(0.4306\) | |||||||
0.02 | \(3.0999\) | \(0.4322\) | |||||||
0.03 | \(3.0922\) | \(0.4341\) | |||||||
0.04 | \(3.0848\) | \(0.4360\) | |||||||
0.02 | \(3.1031\) | \(0.4319\) | |||||||
0.03 | \(3.0984\) | \(0.4336\) | |||||||
0.04 | \(3.0939\) | \(0.4353\) | |||||||
3.7 | \(3.1080\) | \(0.4302\) | |||||||
4.8 | \(3.108\) 0 | \(0.4306\) | |||||||
5.7 | 3.1080 | \(0.4311\) | |||||||
3.7 | 3.1080 | \(0.4305\) | |||||||
4.8 | 3.1080 | \(0.4308\) | |||||||
5.7 | 3.1080 | \(0.4311\) | |||||||
4.5 | 3.1080 | \(0.4485\) | |||||||
5.2 | \(3.108\) 0 | \(0.4409\) | |||||||
5.5 | \(3.108\) 0 | \(0.4376\) |