Metal impregnated activated carbon as cost-effective and scalable catalysts for amine-based CO2 capture

被引:29
作者
Bhatti, Ali Hassan [1 ,2 ]
Waris, Mamoona [3 ,4 ]
Kazmi, Wajahat W. [1 ,2 ]
Bhatti, Umair H. [5 ]
Min, Gwan Hong [1 ,2 ]
Park, Byung Cheol [6 ]
Kweon, Sungjoon [7 ]
Baek, Il Hyun [1 ,2 ]
Nam, Sung Chan [1 ,2 ]
机构
[1] Korea Inst Energy Res, 217 Gajeong Ro, Daejeon 34129, South Korea
[2] Univ Sci & Technol, 217 Gajeong Ro, Daejeon 34113, South Korea
[3] Chungnam Natl Univ, 99 Daehak Ro, Daejeon, South Korea
[4] Grad Sch Energy & Sci Technol, 99 Daehak Ro, Daejeon 35015, South Korea
[5] King Abdullah Univ Sci & Technol, Thuwal 23955, Saudi Arabia
[6] Hyundai Steel, 1480 Bukbusaneop Ro, Dangjin Si 31719, Chungnam, South Korea
[7] Incheon Natl Univ, 119 Acad Ro, Incheon 22012, South Korea
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2023年 / 11卷 / 01期
关键词
CO2; capture; Amine regeneration; Catalytic solvent regeneration; Heat duty; Metal-impregnated activated carbon; SUPPORTED METAL; SOLVENT; DECOMPOSITION; NANOPARTICLES; OPTIMIZATION; PERFORMANCE; MOLYBDENUM; REDUCTION; SEPIOLITE; GAS;
D O I
10.1016/j.jece.2022.109231
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
One of the main challenges of absorption-based CO2 capture hampering its industrial application is the huge energy penalty during solvent regeneration. The addition of a solid acidic catalyst to the solvent regeneration step can optimize the CO2 desorption at low temperatures and hence reduce the significant regeneration penalty. However, as the majority of the studied catalysts are costly, e.g., metal oxides and zeolites, and their addition can negate the benefit of lowered heat duty, the development of cost-effective and abundant materials is paramount. In this regard, we synthesized metal (Fe, Ni, Mo) supported activated carbon (AC) catalysts and evaluated their performance in the regeneration of the benchmark 5 M monoethanolamine (MEA) solution at 86 degrees C. The gathered data show that adding metal-impregnated AC catalysts can greatly improve amine solvent regeneration by boosting the rate of CO2 desorption by 113% and lowering the heat duty by 21.2% when compared to the noncatalytic MEA solution. Catalyst characterization data revealed that the CO2 desorption optimization is primarily governed by the number of acid sites available on the catalyst surface. The experimental results indicate that using scalable and inexpensive materials can significantly reduce the utility requirements for CO2 capture, ultimately advancing catalytic CO2 capture towards industrial implementation.
引用
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页数:12
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