Chinese Journal of Applied Chemistry ›› 2024, Vol. 41 ›› Issue (6): 839-850.DOI: 10.19894/j.issn.1000-0518.240018
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Zhi-Yan LU1, Wen-Xuan CHEN1, Wang-Shi-Yi SUN1, Ning-Ze ZHUO2, Xiao WEI1, Li-Fang LIAO1, Qing-Li XU1, Shi-Yong WU1()
Received:
2024-01-18
Accepted:
2024-04-18
Published:
2024-06-01
Online:
2024-07-09
Contact:
Shi-Yong WU
About author:
wsy@ecust.edu.cnSupported by:
CLC Number:
Zhi-Yan LU, Wen-Xuan CHEN, Wang-Shi-Yi SUN, Ning-Ze ZHUO, Xiao WEI, Li-Fang LIAO, Qing-Li XU, Shi-Yong WU. Preparation of Ce-Mn/ZrO2 Composite Catalyst and Its Sulfur Fixation Performance[J]. Chinese Journal of Applied Chemistry, 2024, 41(6): 839-850.
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URL: http://yyhx.ciac.jl.cn/EN/10.19894/j.issn.1000-0518.240018
Sample | Proximate analysis/%(mass percent) | Ultimate analysis/%(mass percent) | |||||||
---|---|---|---|---|---|---|---|---|---|
Mad | Aad | Vad | FCad | Cdaf | Hdaf | Odaf | Ndaf | Sdaf | |
Sludge | 3.78 | 49.23 | 42.84 | 4.15 | 50.00 | 9.17 | 29.74 | 6.48 | 4.61 |
Table 1 Proximate and ultimate analysis of sludge
Sample | Proximate analysis/%(mass percent) | Ultimate analysis/%(mass percent) | |||||||
---|---|---|---|---|---|---|---|---|---|
Mad | Aad | Vad | FCad | Cdaf | Hdaf | Odaf | Ndaf | Sdaf | |
Sludge | 3.78 | 49.23 | 42.84 | 4.15 | 50.00 | 9.17 | 29.74 | 6.48 | 4.61 |
Sample | Ignition point/℃ | Combustion stage | Corresponding temperature range/℃ | Reaction order n | Fitting equation | Coefficient of determination R2 | E/ (kJ·mol-1) |
---|---|---|---|---|---|---|---|
Sludge | 218.00 | Before volatile peak 1 | 217.66~264.91 | 0.5 | y=-4 054.5x-6.071 9 | 0.963 4 | 33.71 |
After volatile peak 1 | 272.09~300.28 | 2 | y=-4 478.1x-4.757 4 | 0.975 6 | 37.23 | ||
After fixed carbon peak 2 | 400.72~467.43 | 2 | y=-6 627.9x-1.815 2 | 0.995 9 | 55.10 | ||
Sludge-Ca | 212.06 | Before volatile peak 1 | 220.92~263.66 | 0.5 | y=-3 358.7x-7.380 9 | 0.964 0 | 27.92 |
After volatile peak 1 | 275.01~305.03 | 2 | y=-4 358.9x-5.022 9 | 0.985 2 | 36.24 | ||
After fixed carbon peak 2 | 402.13~471.85 | 2 | y=-5 172.6x-4.066 5 | 0.987 3 | 43.01 | ||
Sludge-Ca-C | 206.21 | Before volatile peak 1 | 227.08~261.98 | 0.5 | y=-2 759.5x-8.640 5 | 0.981 0 | 22.94 |
After volatile peak 1 | 286.34~324.70 | 2 | y=-4 025.9x-5.875 0 | 0.993 2 | 33.47 | ||
After fixed carbon peak 2 | 396.46~457.86 | 2 | y=-3596.6x-6.6980 | 0.988 3 | 29.90 |
Table 2 Kinetic parameters for combustion of sludge
Sample | Ignition point/℃ | Combustion stage | Corresponding temperature range/℃ | Reaction order n | Fitting equation | Coefficient of determination R2 | E/ (kJ·mol-1) |
---|---|---|---|---|---|---|---|
Sludge | 218.00 | Before volatile peak 1 | 217.66~264.91 | 0.5 | y=-4 054.5x-6.071 9 | 0.963 4 | 33.71 |
After volatile peak 1 | 272.09~300.28 | 2 | y=-4 478.1x-4.757 4 | 0.975 6 | 37.23 | ||
After fixed carbon peak 2 | 400.72~467.43 | 2 | y=-6 627.9x-1.815 2 | 0.995 9 | 55.10 | ||
Sludge-Ca | 212.06 | Before volatile peak 1 | 220.92~263.66 | 0.5 | y=-3 358.7x-7.380 9 | 0.964 0 | 27.92 |
After volatile peak 1 | 275.01~305.03 | 2 | y=-4 358.9x-5.022 9 | 0.985 2 | 36.24 | ||
After fixed carbon peak 2 | 402.13~471.85 | 2 | y=-5 172.6x-4.066 5 | 0.987 3 | 43.01 | ||
Sludge-Ca-C | 206.21 | Before volatile peak 1 | 227.08~261.98 | 0.5 | y=-2 759.5x-8.640 5 | 0.981 0 | 22.94 |
After volatile peak 1 | 286.34~324.70 | 2 | y=-4 025.9x-5.875 0 | 0.993 2 | 33.47 | ||
After fixed carbon peak 2 | 396.46~457.86 | 2 | y=-3596.6x-6.6980 | 0.988 3 | 29.90 |
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