Table 4 CCD experimental design for the leaching of REEs using citric acid.
Expt. No. | A: Leachant Concentration (mol/L) | B: Reaction Temperature (K) | C: Leaching time (min) | Sc(mg/L) | La(mg/L) | Ce(mg/L) | Pr(mg/L) | Nd(mg/L) | Sm(mg/L) | ⅀REE(mg/L) | REE Leaching efficiency(%) |
|---|---|---|---|---|---|---|---|---|---|---|---|
1 | 0.75 | 343.0 | 240 | 2.909 | 3.022 | 0.559 | 0.429 | 3.174 | 1.015 | 11.108 | 44.50 |
2 | 1.375 | 320.5 | 165 | 2.691 | 4.254 | 0.229 | 0.335 | 3.527 | 0.998 | 12.034 | 48.21 |
3 | 2.43 | 320.5 | 165 | 4.086 | 6.689 | 0.883 | 0.802 | 4.248 | 1.993 | 18.701 | 74.92 |
4 | 0.75 | 298.0 | 90 | 1.579 | 2.142 | 0 | 0 | 2.231 | 0.438 | 6.390 | 25.60 |
5 | 1.375 | 320.5 | 165 | 3.264 | 3.997 | 0.256 | 0.389 | 3.654 | 0.854 | 12.414 | 49.74 |
6 | 1.375 | 320.5 | 165 | 2.994 | 3.884 | 0.257 | 0.415 | 3.224 | 1.005 | 11.779 | 47.19 |
7 | 0.75 | 343.0 | 90 | 2.173 | 2.597 | 0.165 | 0.246 | 2.836 | 0.836 | 8.853 | 35.47 |
8 | 2.00 | 343.0 | 90 | 3.745 | 6.142 | 0.231 | 0.201 | 4.349 | 1.447 | 16.115 | 64.56 |
9 | 1.375 | 320.5 | 291 | 3.781 | 4.408 | 0.449 | 0.411 | 3.983 | 0.997 | 14.029 | 56.21 |
10 | 1.375 | 320.5 | 165 | 3.012 | 3.884 | 0.257 | 0.415 | 3.224 | 1.005 | 11.797 | 47.26 |
11 | 2.00 | 298.0 | 90 | 2.716 | 5.229 | 0.23 | 0.075 | 3.219 | 0.788 | 12.257 | 49.11 |
12 | 1.375 | 320.5 | 165 | 2.784 | 3.657 | 0.221 | 0.409 | 2.891 | 0.884 | 10.846 | 43.45 |
13 | 1.375 | 358.3 | 165 | 4.364 | 5.019 | 0.627 | 0.561 | 4.125 | 1.354 | 16.05 | 64.30 |
14 | 0.32 | 320.5 | 165 | 1.418 | 1.306 | 0.318 | 0.164 | 1.372 | 0.615 | 5.193 | 20.81 |
15 | 0.75 | 298.0 | 240 | 1.785 | 1.949 | 0.226 | 0.12 | 1.965 | 0.507 | 6.552 | 26.25 |
16 | 1.375 | 320.5 | 39 | 2.34 | 2.219 | 0.516 | 0.556 | 2.916 | 1.186 | 9.733 | 38.99 |
17 | 1.375 | 320.5 | 165 | 3.187 | 3.487 | 0.338 | 0.428 | 2.891 | 1.005 | 11.336 | 45.42 |
18 | 2.00 | 343.0 | 240 | 4.784 | 7.954 | 0.848 | 0.724 | 5.748 | 2.447 | 22.505 | 90.16 |
19 | 2.00 | 298.0 | 240 | 3.234 | 5.238 | 0.315 | 0.319 | 4.119 | 1.452 | 14.677 | 58.80 |
20 | 1.375 | 282.7 | 165 | 1.143 | 1.879 | 0 | 0 | 1.883 | 0.784 | 5.689 | 22.79 |