Research Article
A Variational Principle for the Steady-State Heat Transfer Process in a Rigid Continuous Mixture
Table 1
The dimensionless temperatures
and
at the dimensionless positions (
) , and
, obtained with
, , and
, employing
, for four values of
and
(with
).
| ā | ā | | | | | | |
| | | 161.47 87.26 | 160.24 86.53 | 156.48 84.33 | 150.17 80.70 | 141.25 75.68 | 129.63 69.35 | | | 136.18 112.55 | 135.14 111.63 | 131.99 108.83 | 126.69 104.18 | 119.19 97.73 | 109.41 89.58 | | | 126.45 122.28 | 125.46 121.31 | 122.48 118.34 | 117.49 113.38 | 110.47 106.45 | 101.38 97.60 | | | 124.86 123.86 | 123.89 122.89 | 120.91 119.91 | 115.93 114.94 | 108.96 107.97 | 99.97 99.02 |
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