Analysis of Boundary Layer Flow and Heat Transfer along a Stretching Cylinder in a Porous Medium

Table 1

Values of 𝑁𝑢_𝑥Re^𝑥−1/2=−𝜃^/(0) for several values of temperature exponent 𝑁 for flat plate (𝑀=0) in nonporous medium (𝑘₁=0) and 𝑃𝑟=1.

N	Ishak and Nazar [17]	Grubka and Bobba [18]	Ali [19]	Present study
0	0.5820	0.5820	0.5801	0.5821
1	1.0000	1.0000	0.9961	1.0000
2	1.3333	1.3333	1.3269	1.3332