Similarity Solution of Heat and Mass Transfer for Natural Convection over a Moving Vertical Plate with Internal Heat Generation and a Convective Boundary Condition in the Presence of Thermal Radiation, Viscous Dissipation, and Chemical Reaction

Table 2

Computation showing 𝑓^′′(0), 𝜃^′(0), 𝜃(0), and 𝜙^′(0) for different embedded flow parameter values.

Bi	Gr	Gc	Pr	R	Q	Ec	Sc	𝐾𝑟	𝑓^′′(0)	𝜃^′(0)	𝜃(0)	𝜙^′(0)
0.1	1.0	1.0	1.0	0.5	0.1	0.1	0.6	0.5	0.617935	0.0690068	0.309932	0.690904
1.0	1.0	1.0	1.0	0.5	0.1	0.1	0.6	0.5	0.995463	0.24145	0.75855	0.705335
10.0	1.0	1.0	1.0	0.5	0.1	0.1	0.6	0.5	1.16294	0.325667	0.967433	0.71137
0.1	2.0	1.0	1.0	0.5	0.1	0.1	0.6	0.5	0.914867	0.0688259	0.311741	0.703017
0.1	3.0	1.0	1.0	0.5	0.1	0.1	0.6	0.5	1.21966	0.0680544	0.319456	0.714747
0.1	1.0	2.0	1.0	0.5	0.1	0.1	0.6	0.5	1.27296	0.067557	0.32443	0.711755
0.1	1.0	3.0	1.0	0.5	0.1	0.1	0.6	0.5	1.8969	0.064555	0.35445	0.729823
0.1	1.0	1.0	1.0	0.5	0.1	0.1	0.6	0.5	0.598557	0.0696409	0.303591	0.689679
0.1	1.0	1.0	3.0	0.5	0.1	0.1	0.6	0.5	0.537444	0.070888	0.29112	0.685736
0.1	1.0	1.0	1.0	1.0	0.1	0.1	0.6	0.5	0.635229	0.0684205	0.315795	0.691995
0.1	1.0	1.0	1.0	1.5	0.1	0.1	0.6	0.5	0.645997	0.0680532	0.319468	0.692676
0.1	1.0	1.0	1.0	0.5	0.2	0.1	0.6	0.5	0.694807	0.0621171	0.378829	0.694271
0.1	1.0	1.0	1.0	0.5	0.3	0.1	0.6	0.5	0.769222	0.0553443	0.446557	0.697471
0.1	1.0	1.0	1.0	0.5	0.1	0.2	0.6	0.5	0.654059	0.0662619	0.337381	0.692653
0.1	1.0	1.0	1.0	0.5	0.1	0.3	0.6	0.5	0.693151	0.0632311	0.367689	0.694521
0.1	1.0	1.0	1.0	0.5	0.1	0.1	0.78	0.5	0.562746	0.0687271	0.312729	0.786616
0.1	1.0	1.0	1.0	0.5	0.1	0.1	1.0	0.5	0.511741	0.068638	0.311362	0.889928
0.1	1.0	1.0	1.0	0.5	0.1	0.1	0.6	1.0	0.514718	0.0688634	0.311366	0.877011
0.1	1.0	1.0	1.0	0.5	0.1	0.1	0.6	1.5	0.488687	0.0687467	0.312533	1.03195