Mathematical Analysis of Heat Transfer in Peristaltic Transport through a Rough Nonuniform Inclined Channel

Table 3

Temperature distribution at different values of and surface roughness parameter.

0	1	1	1	1	0	0	0	0
0.2	0.9203	0.9173	0.9153	0.9132	0.2839	0.2825	0.2816	0.2807
0.4	0.8319	0.8261	0.8222	0.8179	0.5592	0.5566	0.5548	0.5529
0.6	0.7127	0.7043	0.6986	0.6924	0.8036	0.7999	0.7975	0.7948
0.8	0.5256	0.5151	0.508	0.5003	0.9801	0.9760	0.9732	0.9702
1.0	0.2186	0.2070	0.1992	0.1908	1.0368	1.0331	1.0307	1.0282
0	1	1	1	1	0	0	0	0
0.2	0.8301	0.8289	0.8281	0.8272	0.1938	0.1941	0.1944	0.1947
0.4	0.6593	0.6569	0.6552	0.6534	0.3866	0.3873	0.3878	0.3884
0.6	0.4849	0.4813	0.4789	0.4763	0.5758	0.5770	0.5778	0.5787
0.8	0.3024	0.2979	0.2949	0.2916	0.7570	0.7588	0.7601	0.7615
1.0	0.1059	0.1008	0.0973	0.0936	0.9241	0.9269	0.9289	0.9310
0	1	1	1	1	0	0	0	0
0.2	0.8197	0.8188	0.8182	0.8175	0.1833	0.1840	0.1845	0.1850
0.4	0.6393	0.6375	0.6363	0.6349	0.3666	0.3679	0.3689	0.3699
0.6	0.4585	0.4558	0.4539	0.4519	0.5494	0.5514	0.5528	0.5544
0.8	0.2766	0.2731	0.2707	0.2681	0.7311	0.7339	0.7359	0.7380
1.0	0.0928	0.0886	0.0858	0.0827	0.9110	0.9147	0.9173	0.9201
0	1	1	1	1	0	0	0	0
0.2	0.8182	0.8174	0.8168	0.8162	0.1818	0.1826	0.1831	0.1837
0.4	0.6364	0.6348	0.6337	0.6325	0.3636	0.3652	0.3663	0.3674
0.6	0.4545	0.4522	0.4505	0.4487	0.5455	0.5478	0.5494	0.5512
0.8	0.2727	0.2695	0.2674	0.2650	0.7273	0.7304	0.7326	0.7349
1.0	0.0909	0.0869	0.0842	0.0812	0.9091	0.9130	0.9157	0.9187