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 ).

		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