From: Drying kinetics and mathematical modeling of hot air drying of coconut coir pith
Model | Velocity (m/s) | Model constants | R2 | \({\upchi }^{2} \times 10^{ - 2}\) | RMSE | E% | ||
---|---|---|---|---|---|---|---|---|
a | b × 102 | c × 102 | ||||||
MR = 1 + at + bt 2. (Wang and Singh model) | 2.5 | −0.01282 | 0.002552 | 0.9981 | 0.0297 | 0.0149 | 21.45 | |
2 | −0.01174 | 0.001763 | 0.9977 | 0.0354 | 0.0175 | 23.95 | ||
7 | −0.01118 | 0.001589 | 0.9974 | 0.0430 | 0.0193 | 27.97 | ||
1.4 | −0.01120 | 0.001875 | 0.9959 | 0.0708 | 0.0248 | 54.84 | ||
MR = a + bt (Linear model) | 2.5 | 0.96816 | −1.03312 | 0.9931 | 0.1077 | 0.0284 | 82.19 | |
2 | 0.97749 | −0.99589 | 0.9948 | 0.0782 | 0.0247 | 60.52 | ||
1.7 | 0.98372 | −0.95776 | 0.9938 | 0.0944 | 0.0271 | 69.26 | ||
1.4 | 0.98068 | −0.92965 | 0.9895 | 0.1585 | 0.0351 | 102.52 | ||
\(MR = \frac{{\left( {1 + at + bt^{2} } \right)}}{{\left( {1 + ct} \right)}}\) (proposed model) | 2.5 | −0.01926 | 0.00925 | −0.7306 | 0.9988 | 0.0221 | 0.0111 | 7.26 |
2 | −0.01896 | 0.00899 | −0.7923 | 0.9987 | 0.0241 | 0.0126 | 7.77 | |
1.7 | −0.01827 | 0.00836 | −0.7766 | 0.9987 | 0.0249 | 0.0128 | 16.15 | |
1.4 | −0.01799 | 0.00810 | −0.7677 | 0.9986 | 0.0291 | 0.0149 | 5.67 |