Advances and challenges in electrochemical CO2 reduction processes: an engineering and design perspective looking beyond new catalyst materials

被引:366
作者
Garg, Sahil [1 ]
Li, Mengran [1 ]
Weber, Adam Z. [2 ]
Ge, Lei [1 ,3 ]
Li, Liye [4 ]
Rudolph, Victor [1 ]
Wang, Guoxiong [1 ]
Rufford, Thomas E. [1 ]
机构
[1] Univ Queensland, Sch Chem Engn, St Lucia, Qld 4072, Australia
[2] Lawrence Berkeley Natl Lab, Joint Ctr Articial Photosynth, 1 Cyclotron Rd, Berkeley, CA 94720 USA
[3] Univ Southern Queensland, Ctr Future Mat, Springfield 4300, Australia
[4] HBIS Grp Technol Res Inst, Shijiazhuang, Hebei, Peoples R China
基金
澳大利亚研究理事会;
关键词
GAS-DIFFUSION ELECTRODES; CARBON-DIOXIDE REDUCTION; HIGH-PRESSURE CO2; PEM FUEL-CELLS; ION-EXCHANGE MEMBRANES; FORMIC-ACID; ELECTROCATALYTIC REDUCTION; AQUEOUS-SOLUTIONS; BIPOLAR MEMBRANES; COPPER ELECTRODE;
D O I
10.1039/c9ta13298h
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Electrochemical CO2 reduction (CO2R) is one of several promising strategies to mitigate CO2 emissions. Electrochemical processes operate at mild conditions, can be tuned to selective products, allow modular design, and provide opportunities to integrate renewable electricity with CO2 reduction in carbon-intensive manufacturing industries such as iron and steel making. In recent years, significant advances have been achieved in the development of highly efficient and selective electrocatalysts for CO2R. However, to realize fully the potential benefits of new electrocatalysts in low cost, large scale CO2R electrolyzers requires advances in design and engineering of the CO2R process. In this review, we examine the state-of-the-art in electrochemical CO2R technologies, and highlight how the efficiency of CO2R processes can be improved through (i) electrolyzer configuration, (ii) electrode structure, (iii) electrolyte selection, (iv) pH control, and (v) the electrolyzer's operating pressure and temperature. Although a comprehensive review of catalytic materials is beyond this review's scope, we illustrate how other engineering and design decisions may also influence CO2R reaction pathways because of effects on mass transfer rates, the electrode surface chemistry, interactions with intermediate reaction species, and rates of charge transfer.
引用
收藏
页码:1511 / 1544
页数:34
相关论文
共 353 条
[1]  
48Perry JH., 1950, Chemical Engineers Handbook, V3rd
[2]  
Abdelkader H. S., 2012, INT C ENV BIOM BIOT
[3]   The Electrochemical Reduction of Carbon Dioxide to Formate/Formic Acid: Engineering and Economic Feasibility [J].
Agarwal, Arun S. ;
Zhai, Yumei ;
Hill, Davion ;
Sridhar, Narasi .
CHEMSUSCHEM, 2011, 4 (09) :1301-1310
[4]   Electroreduction of CO2 on polycrystalline copper: Effect of temperature on product selectivity [J].
Ahn, Steven T. ;
Abu-Baker, Ismael ;
Palmore, G. Tayhas R. .
CATALYSIS TODAY, 2017, 288 :24-29
[5]   Carbon Capture and Utilization Update [J].
Al-Mamoori, Ahmed ;
Krishnamurthy, Anirudh ;
Rownaghi, Ali A. ;
Rezaei, Fateme .
ENERGY TECHNOLOGY, 2017, 5 (06) :834-849
[6]   Cu2O-loaded gas diffusion electrodes for the continuous electrochemical reduction of CO2 to methanol [J].
Albo, Jonathan ;
Irabien, Angel .
JOURNAL OF CATALYSIS, 2016, 343 :232-239
[7]   Production of methanol from CO2 electroreduction at Cu2O and Cu2O/ZnO-based electrodes in aqueous solution [J].
Albo, Jonathan ;
Saez, Alfonso ;
Solla-Gullon, Jose ;
Montiel, Vicente ;
Irabien, Angel .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2015, 176 :709-717
[8]  
Alper Erdogan, 2017, Petroleum, V3, P109, DOI 10.1016/j.petlm.2016.11.003
[9]   Ionic liquids in the electrochemical valorisation of CO2 [J].
Alvarez-Guerra, Manuel ;
Albo, Jonathan ;
Alvarez-Guerra, Enrique ;
Irabien, Angel .
ENERGY & ENVIRONMENTAL SCIENCE, 2015, 8 (09) :2574-2599
[10]   Conversion of carbon dioxide into formate using a continuous electrochemical reduction process in a lead cathode [J].
Alvarez-Guerra, Manuel ;
Quintanilla, Sheila ;
Irabien, Angel .
CHEMICAL ENGINEERING JOURNAL, 2012, 207 :278-284