Chemical Industry and Engineering Progress ›› 2022, Vol. 41 ›› Issue (1): 120-132.DOI: 10.16085/j.issn.1000-6613.2021-0114
• Energy processes and technology • Previous Articles Next Articles
Received:
2021-01-18
Revised:
2021-03-30
Online:
2022-01-24
Published:
2022-01-05
Contact:
BAO Cheng
通讯作者:
包成
作者简介:
纪子柯(1997—),男,硕士研究生,研究方向为CO深度去除。E-mail:基金资助:
CLC Number:
JI Zike, BAO Cheng. Research progress of selective CO methanation[J]. Chemical Industry and Engineering Progress, 2022, 41(1): 120-132.
纪子柯, 包成. CO选择性甲烷化的研究进展[J]. 化工进展, 2022, 41(1): 120-132.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2021-0114
催化剂 | 反应气体体积分数/% | 质量空速 | 体积空速 | Tmin | Smin(CO) | Tmax | Smax(CO) | 参考文献 | |||
---|---|---|---|---|---|---|---|---|---|---|---|
CO | CO2 | H2 | H2O | /cm3·h-1·g-1 | /h-1 | /℃ | /% | /℃ | /% | ||
5%Ru/Al2O3 | 0.56 | 21.7 | 42.2 | He | 19800 | 210 | 100 | 244 | 50 | [ | |
Ni/ZrO2 | 1 | 20 | 79 | 0 | 8500 | 215 | 100 | 350 | 50 | [ | |
3%Ru/50%NiAlOx/NF | 1 | 20 | 79 | 0 | 250 | 180 | 100 | 280 | 50 | [ | |
RuNi/Al2O3-CNTs/NF | 1 | 20 | 79 | 0 | 1400 | 190 | 100 | 250 | 50 | [ | |
MS/Ni/AlVOx | 0.43 | 17.1 | 67.9 | 14.53 | 2400 | 170 | 100 | 200 | 50 | [ | |
0.22TMS/0.039V/Ni | 0.43 | 17.1 | 67.9 | 14.53 | 4800 | 164 | 100 | 198 | 50 | [ | |
Ni/CeO2(Cl*) | 1 | 20 | 65 | 10 | 29000 | 240 | 90 | 285 | 50 | [ | |
Ni(Cl0.1)/ZrO2 | 1 | 18 | 70 | N2 | 15000 | 215 | 100 | 295 | 50 | [ | |
Ru-Ni/TiO2-Al2O3 | 1 | 20 | 50 | He | 2400 | 210 | 95 | 220 | 80 | [ | |
1%Ru/MA-40Ni | 0.87 | 17.4 | 68.73 | 13 | 2400 | 190 | 100 | 260 | 50 | [ |
催化剂 | 反应气体体积分数/% | 质量空速 | 体积空速 | Tmin | Smin(CO) | Tmax | Smax(CO) | 参考文献 | |||
---|---|---|---|---|---|---|---|---|---|---|---|
CO | CO2 | H2 | H2O | /cm3·h-1·g-1 | /h-1 | /℃ | /% | /℃ | /% | ||
5%Ru/Al2O3 | 0.56 | 21.7 | 42.2 | He | 19800 | 210 | 100 | 244 | 50 | [ | |
Ni/ZrO2 | 1 | 20 | 79 | 0 | 8500 | 215 | 100 | 350 | 50 | [ | |
3%Ru/50%NiAlOx/NF | 1 | 20 | 79 | 0 | 250 | 180 | 100 | 280 | 50 | [ | |
RuNi/Al2O3-CNTs/NF | 1 | 20 | 79 | 0 | 1400 | 190 | 100 | 250 | 50 | [ | |
MS/Ni/AlVOx | 0.43 | 17.1 | 67.9 | 14.53 | 2400 | 170 | 100 | 200 | 50 | [ | |
0.22TMS/0.039V/Ni | 0.43 | 17.1 | 67.9 | 14.53 | 4800 | 164 | 100 | 198 | 50 | [ | |
Ni/CeO2(Cl*) | 1 | 20 | 65 | 10 | 29000 | 240 | 90 | 285 | 50 | [ | |
Ni(Cl0.1)/ZrO2 | 1 | 18 | 70 | N2 | 15000 | 215 | 100 | 295 | 50 | [ | |
Ru-Ni/TiO2-Al2O3 | 1 | 20 | 50 | He | 2400 | 210 | 95 | 220 | 80 | [ | |
1%Ru/MA-40Ni | 0.87 | 17.4 | 68.73 | 13 | 2400 | 190 | 100 | 260 | 50 | [ |
CO直接解离 | 歧化反应 |
---|---|
CO直接解离 | 歧化反应 |
---|---|
HCO路径 | COH路径 | ||
---|---|---|---|
HCO路径 | COH路径 | ||
---|---|---|---|
反应类型 | 反应方式 | 反应方式判定 | 活性位点位置 | 主要中间体 | 限速步骤 | 影响因素 |
---|---|---|---|---|---|---|
CO甲烷化 | 解离 | C-O键断裂是否 有H协助 | 活性金属 | Cad | Cad的加氢 | 温度、表面结构 |
缔合 | HCOad | HCOad的生成 | ||||
COHad | COHad的生成 | |||||
CO2甲烷化 | 解离 | 是否生成COad中间体 | 活性金属 | COad | COad的解离 | 反应气体组成、制备方法、 活性组分负载量 |
缔合 | 金属-载体作用界面 | COad的生成 | ||||
金属-载体作用界面 | HCOOad | HCOOad的加氢 |
反应类型 | 反应方式 | 反应方式判定 | 活性位点位置 | 主要中间体 | 限速步骤 | 影响因素 |
---|---|---|---|---|---|---|
CO甲烷化 | 解离 | C-O键断裂是否 有H协助 | 活性金属 | Cad | Cad的加氢 | 温度、表面结构 |
缔合 | HCOad | HCOad的生成 | ||||
COHad | COHad的生成 | |||||
CO2甲烷化 | 解离 | 是否生成COad中间体 | 活性金属 | COad | COad的解离 | 反应气体组成、制备方法、 活性组分负载量 |
缔合 | 金属-载体作用界面 | COad的生成 | ||||
金属-载体作用界面 | HCOOad | HCOOad的加氢 |
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