Heat Transfer Analysis for Viscous Fluid Flow with the Newtonian Heating and Effect of Magnetic Force in a Rotating Regime

Table 1

Subjectivity of Nusselt number due to for different values of Pr and S.

	Pr = 1.5	Pr = 2	Pr = 2.5	= 0.3	= 0.5	= 0.7
0.1	1.45893971	1.36332825	1.29323441	1.28798185	1.21272314	1.17518651
0.2	1.46973354	1.37659053	1.30680985	1.28874896	1.21304572	1.17537098
0.3	1.48081222	1.38991945	1.32027242	1.28957462	1.21339402	1.17557059
0.4	1.49221241	1.40339890	1.33369919	1.29044904	1.21376360	1.17578257
0.5	1.50398704	1.41712090	1.34716076	1.29136149	1.21414937	1.17600370
0.6	1.51620697	1.43118859	1.36072051	1.29229999	1.21454580	1.17623089
0.7	1.52897061	1.44571909	1.37443112	1.29325166	1.21494653	1.17646033
0.8	1.54241361	1.46084228	1.38832548	1.29420241	1.21534522	1.17668814
0.9	1.55673282	1.47669347	1.40240685	1.29513598	1.21573466	1.17691038
1.0	1.57222017	1.49339487	1.41663477	1.29603494	1.21610801	1.17712268