Simulation of Thermal Decomposition of Calcium Oxide in a Backward Step Tubular Reactor Containing a Cooling Jacket to Enhance the Heat Transfer and the Rotation Rate

Table 2

Average Nusselt number at the outlet of the channel.

100	71000	1	15.94	6.61	17.88	6.74	21.49	6.96
100	71000	2	14.87	6.52	16.82	6.67	20.57	6.91
100	71000	3	13.93	6.44	15.87	6.60	19.72	6.86
100	73000	1	15.85	6.60	17.79	6.74	21.38	6.95
100	73000	2	14.72	6.51	16.66	6.66	20.38	6.90
100	73000	3	13.75	6.42	15.65	6.58	19.46	6.84
100	75000	1	15.77	6.59	17.69	6.73	21.26	6.95
100	75000	2	14.58	6.50	16.48	6.64	20.15	6.88
100	75000	3	13.56	6.40	15.41	6.56	19.14	6.82
200	71000	1	19.44	9.09	20.78	9.20	23.80	9.42
200	71000	2	17.99	8.95	19.26	9.07	22.07	9.29
200	71000	3	16.78	8.83	18.02	8.95	20.55	9.17
200	73000	1	19.35	9.09	20.68	9.19	23.68	9.41
200	73000	2	17.85	8.94	19.09	9.05	21.85	9.27
200	73000	3	16.61	8.81	17.82	8.93	20.26	9.14
200	75000	1	19.27	9.08	20.59	9.19	23.59	9.41
200	75000	2	17.70	8.93	18.93	9.04	21.67	9.26
200	75000	3	16.41	8.79	17.58	8.91	19.97	9.12
300	71000	1	23.10	11.06	24.73	11.20	26.33	11.32
300	71000	2	21.32	10.89	23.09	11.05	24.55	11.18
300	71000	3	19.85	10.73	21.74	10.92	23.16	11.05
300	73000	1	23.00	11.06	24.61	11.19	26.20	11.32
300	73000	2	21.16	10.88	22.89	11.03	24.32	11.16
300	73000	3	19.65	10.71	21.50	10.89	22.88	11.03
300	75000	1	22.89	11.05	24.48	11.18	26.08	11.31
300	75000	2	20.99	10.86	22.67	11.02	24.09	11.14
300	75000	3	19.43	10.69	21.22	10.87	22.54	11.00
500	71000	1	29.54	14.23	31.97	14.45	33.83	14.61
500	71000	2	27.08	14.00	29.05	14.21	30.91	14.39
500	71000	3	25.04	13.78	26.53	13.98	28.49	14.19
500	73000	1	29.41	14.22	31.84	14.44	33.68	14.60
500	73000	2	26.87	13.98	28.76	14.19	30.56	14.37
500	73000	3	24.76	13.75	26.02	13.94	27.95	14.15
500	75000	1	29.34	14.22	31.87	14.44	33.76	14.61
500	75000	2	26.67	13.96	28.76	14.18	30.52	14.36
500	75000	3	24.54	13.73	26.04	13.93	27.74	14.12