Modified Quasi-Steady Fuel Droplet Combustion Model

Table 3

Proposed model 𝑛-hexane results.

Iteration	𝑇𝑓𝐺 [K]	𝑇^− [K]	𝑘^−g [W/m⋅K]	𝑐^−𝑝g [kJ/kg⋅K]	𝑇^+ [K]	𝑘^+g [W/m⋅K]	𝑐^+𝑝𝑔 [kJ/kg⋅K]	𝐿𝑒^−	𝐿𝑒^+	𝑛	𝐴	𝐵	𝑇𝑓 [K]	𝑟𝑓/𝑟𝑠	K [10^3cm^2/s]	|𝑇𝑓𝐺−𝑇𝑓| [K]
1	2100	1221.0	0.106872	2.6318	1199.0	0.077116	1.1739	2.80	0.82	0.18	0.95	63.43	2349.1	11.79	7.32	249.1
2	2349.1	1345.6	0.114822	3.0807	1323.6	0.085242	1.1968	2.45	0.77	0.17	0.96	68.46	2387.7	10.95	7.83	38.6
3	2387.7	1364.9	0.116093	3.1512	1342.9	0.086586	1.2003	2.41	0.76	0.16	0.96	69.38	2394.6	10.81	7.91	6.9
4	2394.6	1368.3	0.116320	3.1638	1346.3	0.086827	1.2010	2.40	0.76	0.16	0.96	69.54	2395.8	10.79	7.92	1.2

Fixed variables: 𝑇_𝑠=𝑇_boil=342K, 𝑇_∞=298K, 𝜌_𝑙=659 kg/m³, Δℎ_𝑐=45091 kJ/kg, ℎ_𝑓𝑔=355kJ/kg, 𝜐=15.2, 𝜒^−𝐹=0.55,𝜒^−𝑂𝑥=0.45, 𝑌^−𝐹=0.79, 𝑌^−𝑂𝑥=0.21.