Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (6): 3310-3321.DOI: 10.16085/j.issn.1000-6613.2023-0725
• Resources and environmental engineering • Previous Articles
YAN Zhe1(), LIU Chang2(), WANG Fengxu1, ZHOU Hongwang1, LIU Xi2, ZHAO Xuebing2()
Received:
2023-05-04
Revised:
2023-08-07
Online:
2024-07-02
Published:
2024-06-15
Contact:
ZHAO Xuebing
闫哲1(), 刘畅2(), 王丰旭1, 周宏旺1, 刘樨2, 赵雪冰2()
通讯作者:
赵雪冰
作者简介:
闫哲(1987—),男,高级工程师,研究方向为热力系统建模和故障诊断。E-mail:yz_jrhd@126.com基金资助:
CLC Number:
YAN Zhe, LIU Chang, WANG Fengxu, ZHOU Hongwang, LIU Xi, ZHAO Xuebing. Electrochemical reduction of CO2 coupled with oxidative conversion of biomass[J]. Chemical Industry and Engineering Progress, 2024, 43(6): 3310-3321.
闫哲, 刘畅, 王丰旭, 周宏旺, 刘樨, 赵雪冰. 耦合生物质氧化转化的CO2电化学还原[J]. 化工进展, 2024, 43(6): 3310-3321.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2023-0725
还原反应方程式 | 标准电势/V |
---|---|
CO2+e- | -1.90 |
CO2+2H++2e- | -0.53 |
CO2+H2O+2e- | -1.35 |
CO2+2H++2e- | -0.61 |
CO2+H2O+2e- | -1.49 |
CO2+4H++4e- | -0.48 |
CO2+3H2O+4e- | -1.31 |
CO2+6H++6e- | -0.38 |
CO2+5H2O+6e- | -1.23 |
CO2+8H++8e- | -0.24 |
CO2+6H2O+8e- | -1.07 |
CO2+4H++4e- | -2.00 |
CO2+2H2O+4e- | -1.04 |
2CO2+12H++12e- | -0.34 |
2CO2+8H2O+12e- | -1.17 |
2CO2+14H++14e- | -0.27 |
2CO2+2H++2e- | -0.91 |
2CO2+2e- | -1.00 |
2CO2+12H++12e- | -0.33 |
2CO2+9H2O+12e- | -1.16 |
3CO2+18H++18e- | -0.32 |
2H++2e- | -0.42 |
还原反应方程式 | 标准电势/V |
---|---|
CO2+e- | -1.90 |
CO2+2H++2e- | -0.53 |
CO2+H2O+2e- | -1.35 |
CO2+2H++2e- | -0.61 |
CO2+H2O+2e- | -1.49 |
CO2+4H++4e- | -0.48 |
CO2+3H2O+4e- | -1.31 |
CO2+6H++6e- | -0.38 |
CO2+5H2O+6e- | -1.23 |
CO2+8H++8e- | -0.24 |
CO2+6H2O+8e- | -1.07 |
CO2+4H++4e- | -2.00 |
CO2+2H2O+4e- | -1.04 |
2CO2+12H++12e- | -0.34 |
2CO2+8H2O+12e- | -1.17 |
2CO2+14H++14e- | -0.27 |
2CO2+2H++2e- | -0.91 |
2CO2+2e- | -1.00 |
2CO2+12H++12e- | -0.33 |
2CO2+9H2O+12e- | -1.16 |
3CO2+18H++18e- | -0.32 |
2H++2e- | -0.42 |
产物 | 催化剂 | 法拉第效率/% | 过电势/V | 电流密度/mA·cm-2 | 电解液 |
---|---|---|---|---|---|
HCOOH | Pb | 97.4 | -1.19 | 5.0 | 0.1mol/L KHCO3 |
Sn | 88.4 | -1.04 | 5.0 | 0.1mol/L KHCO3 | |
Pd/C | 99 | -0.15 | 2.4~7.0 | 2.8mol/L KHCO3 | |
Pd70Pt30/C | 90 | -0.36 | 4.0~7.5 | 0.2mol/L PO43– | |
CO | Au | 87.1 | -0.64 | 5 | 0.1mol/L KHCO3 |
Au NPs | 97 | -0.58 | 3.49 ± 0.61 | 0.1mol/L KHCO3 | |
OD-Au | >96 | -0.25 | 2~4 | 0.5mol/L NaHCO3 | |
Ag | 94 | -0.99 | 约5 | 0.1mol/L KHCO3 | |
CH4 | 铜箔 | 40.4 | -1.34 | 约7 | 0.1mol/L KHCO3 |
Cu(210) | 64 | -1.29 | 5 | 0.1mol/L KHCO3 | |
C2H4 | 铜箔 | 26.0 | -1.13 | 1~2 | 0.1mol/L KHCO3 |
Cu | 60 | -0.98 | 约15 | 0.1mol/L KHCO3 | |
卤化铜 | 60.5~79.5 | -2.11 | 46.1~39.2 | 3mol/L KBr | |
石墨/碳 NPs/Cu/PTFE | 70 | -0.63 | 75~100 | 7mol/L KOH | |
CH3OH | Cu2O | 38 | -0.43 | 1~2 | 0.5mol/L KHCO3 |
Mo | 84 | -0.33 | 0.12 | 0.2mol/L Na2SO4 | |
C2H5OH | 铜箔 | 9.8 | -1.14 | 约0.6 | 0.1mol/L KHCO3 |
Cu2O | 9~16 | -1.08 | 30~35 | 0.1mol/L KHCO3 | |
CuO | 36.1 | — | 约11.7 | 0.2mol/L KI | |
Cu/CNS | 63 | -1.29 | 2 | 0.1mol/L KHCO3 |
产物 | 催化剂 | 法拉第效率/% | 过电势/V | 电流密度/mA·cm-2 | 电解液 |
---|---|---|---|---|---|
HCOOH | Pb | 97.4 | -1.19 | 5.0 | 0.1mol/L KHCO3 |
Sn | 88.4 | -1.04 | 5.0 | 0.1mol/L KHCO3 | |
Pd/C | 99 | -0.15 | 2.4~7.0 | 2.8mol/L KHCO3 | |
Pd70Pt30/C | 90 | -0.36 | 4.0~7.5 | 0.2mol/L PO43– | |
CO | Au | 87.1 | -0.64 | 5 | 0.1mol/L KHCO3 |
Au NPs | 97 | -0.58 | 3.49 ± 0.61 | 0.1mol/L KHCO3 | |
OD-Au | >96 | -0.25 | 2~4 | 0.5mol/L NaHCO3 | |
Ag | 94 | -0.99 | 约5 | 0.1mol/L KHCO3 | |
CH4 | 铜箔 | 40.4 | -1.34 | 约7 | 0.1mol/L KHCO3 |
Cu(210) | 64 | -1.29 | 5 | 0.1mol/L KHCO3 | |
C2H4 | 铜箔 | 26.0 | -1.13 | 1~2 | 0.1mol/L KHCO3 |
Cu | 60 | -0.98 | 约15 | 0.1mol/L KHCO3 | |
卤化铜 | 60.5~79.5 | -2.11 | 46.1~39.2 | 3mol/L KBr | |
石墨/碳 NPs/Cu/PTFE | 70 | -0.63 | 75~100 | 7mol/L KOH | |
CH3OH | Cu2O | 38 | -0.43 | 1~2 | 0.5mol/L KHCO3 |
Mo | 84 | -0.33 | 0.12 | 0.2mol/L Na2SO4 | |
C2H5OH | 铜箔 | 9.8 | -1.14 | 约0.6 | 0.1mol/L KHCO3 |
Cu2O | 9~16 | -1.08 | 30~35 | 0.1mol/L KHCO3 | |
CuO | 36.1 | — | 约11.7 | 0.2mol/L KI | |
Cu/CNS | 63 | -1.29 | 2 | 0.1mol/L KHCO3 |
阴极CO2电化学还原反应 | 电流密度 /mA·cm-2 | 阳极反应 | 电压 /V | |||
---|---|---|---|---|---|---|
催化剂 | 生成产物 | 法拉第效率/% | 催化剂 | 反应底物 | ||
Ag GDL | CO | 100.9 | 2.29 | Pt | 甘油 | 0.9 |
Ag GDL | CO | 98.85 | 4.55 | Pt | 葡萄糖 | 1.2 |
Sn GDL | HCOOH | 85.5 | 82.52 | Pt | 甘油 | 2.3 |
Sn GDL | HCOOH | 86.39 | 52.46 | Pt | 葡萄糖 | 1.4 |
阴极CO2电化学还原反应 | 电流密度 /mA·cm-2 | 阳极反应 | 电压 /V | |||
---|---|---|---|---|---|---|
催化剂 | 生成产物 | 法拉第效率/% | 催化剂 | 反应底物 | ||
Ag GDL | CO | 100.9 | 2.29 | Pt | 甘油 | 0.9 |
Ag GDL | CO | 98.85 | 4.55 | Pt | 葡萄糖 | 1.2 |
Sn GDL | HCOOH | 85.5 | 82.52 | Pt | 甘油 | 2.3 |
Sn GDL | HCOOH | 86.39 | 52.46 | Pt | 葡萄糖 | 1.4 |
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