Inorganic Chemicals Industry ›› 2022, Vol. 54 ›› Issue (1): 77-82.doi: 10.19964/j.issn.1006-4990.2021-0163
• Environment·Health·Safety • Previous Articles Next Articles
ZHOU Jiaqi(),CHEN Kui(
),WU Bin,JI Lijun,WU Yanyang
Received:
2021-03-18
Online:
2022-01-10
Published:
2022-03-14
Contact:
CHEN Kui
E-mail:jiaqizhou77@163.com.cn;chenkui@ecust.edu.cn
CLC Number:
ZHOU Jiaqi,CHEN Kui,WU Bin,JI Lijun,WU Yanyang. Study on kinetics of phosphate tailings calcination and acid leaching process[J]. Inorganic Chemicals Industry, 2022, 54(1): 77-82.
Table 3
α-T data of thermal decomposition of dolomite in phosphorus tailings at different heating rates"
反应 分解率 | 热分解温度点/K | |||
---|---|---|---|---|
5 K/min | 10 K/min | 15 K/min | 20 K/min | |
0.1 | 876 | 912 | 920 | 919 |
0.2 | 928 | 974 | 979 | 980 |
0.3 | 951 | 997 | 1 000 | 1 004 |
0.4 | 967 | 1 010 | 1 011 | 1 018 |
0.5 | 978 | 1 020 | 1 021 | 1 029 |
0.6 | 987 | 1 031 | 1 033 | 1 039 |
0.7 | 994 | 1 041 | 1 042 | 1 048 |
0.8 | 1 001 | 1 049 | 1 051 | 1 058 |
0.9 | 1 008 | 1 057 | 1 059 | 1 068 |
1.0 | 1 272 | 1 271 | 1 232 | 1 264 |
Table 4
Fitting results of kinetic parameters of dolomite thermal decomposition in phosphorus tailings"
β/ (K·min-1) | 模型 序号 | E/ (kJ·mol-1) | ln A | R2 | 模型 序号 | E/ (kJ·mol-1) | ln A | R2 | 模型 序号 | E/ (kJ·mol-1) | ln A | R2 |
---|---|---|---|---|---|---|---|---|---|---|---|---|
5 | 1 | 205.996 | 23.068 7 | 0.955 0 | 4 | 57.935 | 3.738 3 | 0.938 9 | 7 | 372.306 | 41.369 8 | 0.976 3 |
2 | 310.632 | 36.918 0 | 0.883 1 | 5 | 39.427 | 1.095 7 | 0.927 2 | 8 | 165.480 | 16.934 2 | 0.996 5 | |
3 | 94.950 | 8.747 8 | 0.947 9 | 6 | 281.236 | 31.513 2 | 0.982 1 | 9 | 178.105 | 18.231 5 | 0.974 3 | |
10 | 1 | 222.211 | 24.518 1 | 0.976 1 | 4 | 62.811 | 4.675 0 | 0.967 8 | 7 | 399.895 | 43.236 3 | 0.990 2 |
2 | 337.876 | 39.096 2 | 0.916 4 | 5 | 42.887 | 1.971 0 | 0.961 8 | 8 | 177.633 | 18.124 3 | 0.993 8 | |
3 | 102.661 | 9.811 2 | 0.972 4 | 6 | 300.066 | 32.845 2 | 0.997 2 | 9 | 191.503 | 19.500 0 | 0.989 4 | |
15 | 1 | 232.409 | 26.101 2 | 0.985 5 | 4 | 66.169 | 5.505 3 | 0.980 7 | 7 | 417.146 | 45.597 0 | 0.995 2 |
2 | 354.270 | 41.377 8 | 0.934 4 | 5 | 45.389 | 2.710 9 | 0.977 3 | 8 | 185.512 | 19.445 7 | 0.997 1 | |
3 | 107.729 | 10.827 6 | 0.983 3 | 6 | 312.251 | 34.635 6 | 0.993 9 | 9 | 200.098 | 20.902 2 | 0.994 8 | |
20 | 1 | 215.588 | 24.188 5 | 0.980 7 | 4 | 60.515 | 4.989 6 | 0.973 8 | 7 | 388.331 | 42.168 3 | 0.992 2 |
2 | 328.412 | 38.330 5 | 0.926 9 | 5 | 41.131 | 2.362 4 | 0.968 7 | 8 | 172.139 | 17.966 4 | 0.994 8 | |
3 | 99.283 | 9.966 8 | 0.977 6 | 6 | 291.095 | 32.170 4 | 0.994 8 | 9 | 185.655 | 19.288 4 | 0.991 6 |
Table 5
Fitting result of chemical reaction model and diffusion control model"
反应 温度/K | 化学反应控制模型 | 内扩散控制模型 | ||
---|---|---|---|---|
k1/10-1 | R12 | k2/10-3 | R22 | |
313 | 0.016 8 | 0.950 9 | 0.544 9 | 0.947 5 |
323 | 0.018 4 | 0.949 4 | 0.602 7 | 0.947 7 |
333 | 0.020 8 | 0.947 3 | 0.685 7 | 0.942 6 |
343 | 0.023 3 | 0.941 7 | 0.773 8 | 0.940 6 |
353 | 0.029 2 | 0.940 4 | 0.988 8 | 0.938 3 |
Table 7
Fitting result of chemical reaction model and diffusion control model"
反应 温度/K | 化学反应控制模型 | 内扩散控制模型 | ||
---|---|---|---|---|
k1/10-1 | R12 | k2/10-3 | R22 | |
313 | 0.016 4 | 0.990 9 | 0.569 8 | 0.990 7 |
323 | 0.016 8 | 0.986 5 | 0.592 4 | 0.986 8 |
333 | 0.022 9 | 0.998 9 | 0.853 5 | 0.994 5 |
343 | 0.028 1 | 0.997 9 | 1.120 | 0.992 6 |
353 | 0.033 7 | 0.994 5 | 1.460 | 0.993 9 |
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