Modeling Performance of High-Temperature Biomass Gasification Process

Table 2

The value of ℎ^𝑂_𝑓 (kJ/mol) and coefficients of the empirical equation for Δ𝑔^𝑂_𝑓,𝑇 (kJ/mol).

Compound	ℎ^𝑂𝑓	𝑎^′	𝑏^′	𝑐^′	𝑑^′	𝑒^′	𝑓^′	𝑔^′
CO	−110.5	5.619×10^−3	−1.90×10^−5	6.383×10^−9	−1.846×10^−12	−4.891×10^2	8.684×10^−1	−6.131×10^−2
CO2	−393.5	−1.949×10^−2	3.122×10^−5	−2.448×10^−8	6.946×10^−12	−4.891×10^2	5.270	−1.207×10^−1
H2O	−241.8	−8.950×10^−3	−3.672×10^−6	5.209×10^−9	−1.478×10^−12	0.0	2.868	−1.722×10^−2
CH4	−74.8	−4.620×10^−2	1.130×10^−5	1.319×10^−8	−6.647×10^−12	−4.891×10^2	1.411×10^1	−2.234×10^−1