Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (9): 4951-4960.DOI: 10.16085/j.issn.1000-6613.2023-1340
• Industrial catalysis • Previous Articles
FU Wei1(), NING Shuying1, CAI Chen1, CHEN Jiayin1, ZHOU Hao2, SU Yaxin1()
Received:
2023-08-07
Revised:
2023-12-20
Online:
2024-09-30
Published:
2024-09-15
Contact:
SU Yaxin
付维1(), 宁淑英1, 蔡晨1, 陈佳音1, 周皞2, 苏亚欣1()
通讯作者:
苏亚欣
作者简介:
付维(2000—),男,硕士研究生,研究方向为燃烧污染物控制。E-mail:fuwei2000117@163.com。
基金资助:
CLC Number:
FU Wei, NING Shuying, CAI Chen, CHEN Jiayin, ZHOU Hao, SU Yaxin. SCR-C3H6 denitrification performance of Cu-modified MIL-100(Fe) catalysts[J]. Chemical Industry and Engineering Progress, 2024, 43(9): 4951-4960.
付维, 宁淑英, 蔡晨, 陈佳音, 周皞, 苏亚欣. Cu改性MIL-100(Fe)催化剂的SCR-C3H6脱硝特性[J]. 化工进展, 2024, 43(9): 4951-4960.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2023-1340
催化剂 | 比表面积/m2·g-1 | 孔容/cm3·g-1 | 孔径/nm |
---|---|---|---|
MIL-100(Fe) | 1126 | 0.661 | 2.348 |
2.3Cu-MIL-100(Fe) | 1206 | 1.072 | 3.555 |
3.9Cu-MIL-100(Fe) | 766.2 | 0.616 | 3.215 |
催化剂 | 比表面积/m2·g-1 | 孔容/cm3·g-1 | 孔径/nm |
---|---|---|---|
MIL-100(Fe) | 1126 | 0.661 | 2.348 |
2.3Cu-MIL-100(Fe) | 1206 | 1.072 | 3.555 |
3.9Cu-MIL-100(Fe) | 766.2 | 0.616 | 3.215 |
催化剂 | 结合能/eV | 原子分数/% | ||||||
---|---|---|---|---|---|---|---|---|
Fe3+A | Fe3+B | Cu2+ | Cu+ | Fe3+A | Fe3+B | Cu2+ | Cu+ | |
MIL-100(Fe) | 711.3 | 713.4 | — | — | 58.42 | 41.58 | — | — |
2.3Cu-MIL-100(Fe) | 712.1 | 714.3 | 934.8 | 933.1 | 64.68 | 35.32 | 35.11 | 64.89 |
955.2 | 953.1 | |||||||
3.9Cu-MIL-100(Fe) | 711.0 | 712.9 | 934.5 | 933.0 | 56.95 | 43.05 | 41.85 | 58.15 |
955.3 | 952.9 |
催化剂 | 结合能/eV | 原子分数/% | ||||||
---|---|---|---|---|---|---|---|---|
Fe3+A | Fe3+B | Cu2+ | Cu+ | Fe3+A | Fe3+B | Cu2+ | Cu+ | |
MIL-100(Fe) | 711.3 | 713.4 | — | — | 58.42 | 41.58 | — | — |
2.3Cu-MIL-100(Fe) | 712.1 | 714.3 | 934.8 | 933.1 | 64.68 | 35.32 | 35.11 | 64.89 |
955.2 | 953.1 | |||||||
3.9Cu-MIL-100(Fe) | 711.0 | 712.9 | 934.5 | 933.0 | 56.95 | 43.05 | 41.85 | 58.15 |
955.3 | 952.9 |
催化剂 | 温度/℃ | H2消耗量/mmol·g-1 | ||||||||
---|---|---|---|---|---|---|---|---|---|---|
F1 | F2 | F3 | F4 | F5 | F1 | F2 | F3 | F4 | F5 | |
3.9MIL-100(Fe) | 295 | 385 | 460 | 565 | 715 | 0.039 | 0.457 | 1.252 | 0.303 | 0.205 |
2.3MIL-100(Fe) | 295 | 370 | 445 | 565 | 700 | 0.093 | 0.305 | 1.528 | 0.231 | 0.235 |
MIL-100(Fe) | — | — | 490 | 565 | 730 | — | — | 0.052 | 0.022 | 0.011 |
CuO | 535 | 12.640 |
催化剂 | 温度/℃ | H2消耗量/mmol·g-1 | ||||||||
---|---|---|---|---|---|---|---|---|---|---|
F1 | F2 | F3 | F4 | F5 | F1 | F2 | F3 | F4 | F5 | |
3.9MIL-100(Fe) | 295 | 385 | 460 | 565 | 715 | 0.039 | 0.457 | 1.252 | 0.303 | 0.205 |
2.3MIL-100(Fe) | 295 | 370 | 445 | 565 | 700 | 0.093 | 0.305 | 1.528 | 0.231 | 0.235 |
MIL-100(Fe) | — | — | 490 | 565 | 730 | — | — | 0.052 | 0.022 | 0.011 |
CuO | 535 | 12.640 |
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