Boundary Layer Flow of Second Grade Fluid in a Cylinder with Heat Transfer

Table 1

Behavior of shear stress at the surface for different values of the involved parameters.

	b\γ	𝑓^′′(0)
		0.5	1.0	1.5	2.0	2.5	3.0
β = 0	−1	0.9918	1.1942	1.3729	1.5325	1.6763	1.8067
	0	1.4886	1.7244	1.7954	1.9378	2.0656	2.1810
	1	2.0397	2.1751	2.2982	2.4099	2.5116	2.6044
	2	2.7332	2.8029	2.8746	2.9448	3.0119	3.0752
β = 0.2	−1	0.8626	0.9205	0.95554	0.9794	0.9958	1.0081
	0	1.5946	1.9137	2.0439	2.2662	2.4626	2.6302
	1	4.2201	5.1146	6.8718	9.1792	11.8742	14.465
	2	8.4914	11.7713	15.6358	24.547	29.4885	38.1896
β = 0.4	−1	0.7798	0.7935	0.7970	0.80716	0.80754	0.8077
	0	1.5822	1.8917	2.0213	2.2349	2.4119	2.6165
	1	4.5183	6.7654	8.7508	12.368	16.0122	24.2009
	2	9.0899	14.1113	19.8594	28.5561	35.0772	46.7566