Table 3 Heat transfer rate outcomes comparison for pure fluid with \(\alpha =0\) and \(\lambda =1, M=0\).
Pr | φ | Wang25 | Liu et al.39 | Nadeem et al.35 | Present work |
|---|---|---|---|---|---|
1 | 0 | 0.27741 | 0.27741 | 0.27741 | 0.27741 |
0.1 | − 0.4496 | − 0.4496 | − 0.4496 | − 0.4496 | |
0.3 | − 0.8547 | − 0.8547 | − 0.8547 | − 0.8547 | |
0.4 | − 1.4602 | − 1.4602 | − 1.4602 | − 1.4602 | |
5 | 0 | 1.3532 | 1.3532 | 1.3532 | 1.3532 |
0.1 | − 1.4212 | − 1.4212 | − 1.4212 | − 1.4212 | |
0.3 | − 1.7001 | − 1.7001 | − 1.7001 | − 1.7001 | |
0.4 | − 1.8021 | − 1.8021 | − 1.8021 | − 1.8021 |
