无机材料学报 ›› 2026, Vol. 41 ›› Issue (4): 500-508.DOI: 10.15541/jim20250211 CSTR: 32189.14.10.15541/jim20250211
薛新燕1,2(
), 张晓卫1,2, 鲁恒1,2, 李世杰1,2, 张卫珂1,2(
), 曾少华2,3
收稿日期:2025-05-15
修回日期:2025-09-23
出版日期:2026-04-20
网络出版日期:2025-10-17
通讯作者:
张卫珂, 副教授. E-mail: zhangweike@tyut.edu.cn作者简介:薛新燕(2000-), 女, 硕士研究生. E-mail: 17336334425@163.com
基金资助:
XUE Xinyan1,2(
), ZHANG Xiaowei1,2, LU Heng1,2, LI Shijie1,2, ZHANG Weike1,2(
), CHAN Siewhwa2,3
Received:2025-05-15
Revised:2025-09-23
Published:2026-04-20
Online:2025-10-17
Contact:
ZHANG Weike, associate professor. E-mail: zhangweike@tyut.edu.cnAbout author:XUE Xinyan (2000-), female, Master candidate. E-mail: 17336334425@163.com
Supported by:摘要:
氨分解制氢作为一种极具前景的氢气制备方法, 其关键在于开发具有高活性、高选择性和低成本的中低温催化剂。本研究以甲烷850 ℃裂解制氢副产物纳米洋葱碳(CNOs)为载体, 采用均匀沉积沉淀法负载活性金属钴(Co), 并引入碱金属氧化镁(MgO)作助剂, 成功制备了高性能氨分解催化剂。通过系统研究酸洗及钾(K)活化处理对CNOs载体形貌的调控作用, 深入探究了其对催化剂性能的影响机制。多种表征与化学吸附实验证实, 催化剂碱性强度与其氨分解性能呈正相关。引入CNOs显著提升了催化剂的电子导电性, 并促进了Co2MgO4纳米颗粒在载体上的均匀分散。这种均匀分散增加了碱性活性位点的暴露度, 从而增强了催化剂表面对氨分子的吸附能力。酸洗处理在CNOs表面引入了更多含氧官能团, 这些官能团可作为锚定位点, 与Co2+或Mg2+形成强化学键(配位键或离子键), 进而稳定Co2MgO4颗粒。这种强相互作用提高了金属氧化物的还原难度, 导致其还原温度升高。催化性能测试表明, CNOs、MgO、K和Co的协同作用显著优化了催化剂的结构特性、金属粒径及催化性能。在一系列合成催化剂中, Co2Mg/K-CNO’展现出最优异的氨分解催化活性, 在12000 mL·gcat-1·h-1、550 ℃条件下氨转化率为99.6%。
中图分类号:
薛新燕, 张晓卫, 鲁恒, 李世杰, 张卫珂, 曾少华. 钴-镁协同纳米洋葱碳催化剂的制备及低温催化氨分解制氢性能[J]. 无机材料学报, 2026, 41(4): 500-508.
XUE Xinyan, ZHANG Xiaowei, LU Heng, LI Shijie, ZHANG Weike, CHAN Siewhwa. Co-Mg Synergistic Carbon Nano Onions Catalyst: Preparation and Low-temperature Catalytic Hydrogen Production from Ammonia Decomposition[J]. Journal of Inorganic Materials, 2026, 41(4): 500-508.
| Catalyst | BET specific surface area/ (m2·g-1) | Micropore volume/ (cm3·g-1) | Micropore area/ (m2·g-1) | Average pore size/nm | Co content/% (in mass) |
|---|---|---|---|---|---|
| Co2Mg | 12.7434 | 0.002212 | 6.0318 | 14.6403 | 50 |
| Co2Mg/CNO | 23.4634 | 0.002876 | 6.0278 | 19.4730 | 29 |
| Co2Mg/CNO’ | 23.4880 | 0.003788 | 8.6815 | 20.0063 | 29 |
| Co2Mg/K-CNO | 28.5727 | 0.002307 | 4.8487 | 18.2552 | 29 |
| Co2Mg/K-CNO’ | 34.8266 | 0.002539 | 8.6815 | 17.6383 | 29 |
表1 不同催化剂的比表面积和孔结构参数
Table 1 Specific surface area and pore structure parameters of different catalysts
| Catalyst | BET specific surface area/ (m2·g-1) | Micropore volume/ (cm3·g-1) | Micropore area/ (m2·g-1) | Average pore size/nm | Co content/% (in mass) |
|---|---|---|---|---|---|
| Co2Mg | 12.7434 | 0.002212 | 6.0318 | 14.6403 | 50 |
| Co2Mg/CNO | 23.4634 | 0.002876 | 6.0278 | 19.4730 | 29 |
| Co2Mg/CNO’ | 23.4880 | 0.003788 | 8.6815 | 20.0063 | 29 |
| Co2Mg/K-CNO | 28.5727 | 0.002307 | 4.8487 | 18.2552 | 29 |
| Co2Mg/K-CNO’ | 34.8266 | 0.002539 | 8.6815 | 17.6383 | 29 |
图7 催化剂氨分解活性对比
Fig. 7 Comparison of catalytic activity for ammonia decomposition (a) Co-Mg synergy; (b) K-activated carriers; (c) Different ratios of Co-Mg
| Catalyst | Temperature/℃ | GHSV/(mL·gcat-1·h-1) | NH3 conversion/% | Ref. |
|---|---|---|---|---|
| Co2Mg/K-CNO’ | 550 | 12000 | 99.6 | This work |
| 20CoNaTi-NT | 550 | 6000 | 41 | [ |
| 35%Co/SiC-700 | 550 | 30000 | 78.3 | [ |
| CoOx@C-700A | 500 | 15000 | 55 | [ |
| 90CoAl | 500 | 30000 | 37.8 | [ |
| Co/CNTs | 500 | 6000 | 61 | [ |
| Co-Mo/SiO2-Cap | 500 | 6000 | 20 | [ |
| Co/CeO2 | 500 | 6000 | 62 | [ |
| 26Co-CAT(A) | 500 | 6000 | 58 | [ |
| Fe/CNTs | 500 | 6000 | 15 | [ |
| Co/MWCNTs | 500 | 6000 | 74.6 | [ |
表2 Co基催化剂氨分解性能
Table 2 Catalytic performance of Co-based catalysts for ammonia decomposition
| Catalyst | Temperature/℃ | GHSV/(mL·gcat-1·h-1) | NH3 conversion/% | Ref. |
|---|---|---|---|---|
| Co2Mg/K-CNO’ | 550 | 12000 | 99.6 | This work |
| 20CoNaTi-NT | 550 | 6000 | 41 | [ |
| 35%Co/SiC-700 | 550 | 30000 | 78.3 | [ |
| CoOx@C-700A | 500 | 15000 | 55 | [ |
| 90CoAl | 500 | 30000 | 37.8 | [ |
| Co/CNTs | 500 | 6000 | 61 | [ |
| Co-Mo/SiO2-Cap | 500 | 6000 | 20 | [ |
| Co/CeO2 | 500 | 6000 | 62 | [ |
| 26Co-CAT(A) | 500 | 6000 | 58 | [ |
| Fe/CNTs | 500 | 6000 | 15 | [ |
| Co/MWCNTs | 500 | 6000 | 74.6 | [ |
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