Simulation analysis of integrated amine-based carbon capture and electrochemical conversion utilization
QIU Dongya;ZHAO Chuanwen;JIN Dongling;GUO Yafei;
Abstract:
Excessive CO_2 emissions have triggered a severe climate crisis,with emissions from coal-fired power plants accounting for a significant proportion. Hence, research into flue gas carbon capture has become critical. Chemical absorption, due to its mature technology, holds promise as one of the technologies for large-scale carbon emission reduction applications. However, its further development is constrained by high energy consumption and investment costs. In traditional Carbon Capture and Utilization(CCU)processes,the capture and utilization steps are often conducted separately. Researchers have optimized the capture process by developing new absorbents and energy-saving processes while also developing more efficient and secure CO_2 utilization and storage technologies.However,individually optimizing each process leads to diminishing returns in energy efficiency. Therefore,researchers are considering the economic and energy benefits of integrating carbon capture and utilization technologies. Some scholars propose using electrochemical conversion instead of traditional absorbents for regenerating towers, integrating CO_2 capture and electrochemical conversion for utilization. Based on traditional MEA wet capture processes,a modeling analysis of Integrated Carbon Capture and Utilization(ICCU)using organic amine electrolytes was conducted using Aspen Plus, and a technical and economic analysis of the two processes was performed. The results show that compared to conventional CCU processes,the ICCU process improves CO_2 conversion rates and CO yields by 6% and 33%,respectively. Additionally,the energy efficiency of the ICCU process(38.94%) is slightly higher than that of the CCU process(37.8%). However, with the corresponding increase in electrolysis energy consumption, the overall improvement in energy efficiency is not significant. Sensitivity analysis of the electrolysis temperature reveals a decreasing trend in energy efficiency for both processes with increasing temperature,although the efficiency of the ICCU process remains higher. Moreover,the cost of the ICCU process increases continuously,with a temperature increase of 5°C resulting in a 2% cost increase. Overall,the ICCU process has certain advantages in terms of total cost(6 399.17 yuan/t),with a reduction in system energy consumption being a key factor in further cost reduction. In conclusion,the ICCU process achieves some improvement in economic and energy benefits.
Key Words: electrochemistry;wet scrubbing;carbon capture and utilization;process analysis;Aspen Plus simulation
Foundation: 国家自然科学基金资助项目(52276120)
Authors: QIU Dongya;ZHAO Chuanwen;JIN Dongling;GUO Yafei;
DOI: 10.13226/j.issn.1006-6772.23122001
References:
- [1]IEA.Special report on carbon capture utilization and storage[R/OL].Energy Technology Perspectives 2020,2020.
- [2]LI B Y,DUAN Y H,LUEBKE D,et al.Advances in CO2 capture technology:A patent review[J].Applied Energy,2013,102:1439-1447.
- [3]LEUNG D Y C,CARAMANNA G,MAROTO-VALER M M.An overview of current status of carbon dioxide capture and storage technologies[J].Renewable and Sustainable Energy Reviews,2014,39:426-443.
- [4]BOOT-HANDFORD M E,ABANADES J C,ANTHONY E J,et al.Carbon capture and storage update[J].Energy&Environmental Science,2014,7(1):130-189.
- [5]JIANG K,ASHWORTH P,ZHANG S Y,et al.China’s carbon capture,utilization and storage (CCUS) policy:A critical review[J].Renewable and Sustainable Energy Reviews,2020,119:109601.
- [6]PALTSEV S,MORRIS J,KHESHGI H,et al.Hard-to-abate sectors:The role of industrial carbon capture and storage(CCS)in emission mitigation[J].Applied Energy,2021,300:117322.
- [7]MARTIN-ROBERTS E,SCOTT V,FLUDE S,et al.Carbon capture and storage at the end of a lost decade[J].One Earth,2021,4(11):1569-1584.
- [8]MACDOWELL N,FLORIN N,BUCHARD A,et al.An overview of CO2 capture technologies[J].Energy&Environmental Science,2010,3(11):1645-1669.
- [9]BUI M,ADJIMAN C S,BARDOW A,et al.Carbon capture and storage (CCS):The way forward[J].Energy&Environmental Science,2018,11(5):1062-1176.
- [10]GREENHALGH M D,THOMAS S P.Iron-catalyzed,highly regioselective synthesis of α-aryl carboxylic acids from styrene derivatives and CO2[J].Journal of the American Chemical Society,2012,134(29):11900-11903.
- [11]DE LUNA P,HAHN C,HIGGINS D,et al.What would it take for renewably powered electrosynthesis to displace petrochemical processes?[J].Science,2019,364(6438):eaav3506.
- [12]GARCíA DE ARQUER F P,DINH C T,OZDEN A,et al.CO2electrolysis to multicarbon products at activities greater than 1 Acm-2[J].Science,2020,367(6478):661-666.
- [13]HIGGINS D,HAHN C,XIANG C X,et al.Gas-diffusion electrodes for carbon dioxide reduction:A new paradigm[J].ACSEnergy Letters,2019,4(1):317-324.
- [14]GUTIéRREZ-SáNCHEZ O,BOHLEN B,DAEMS N,et al.A.state-of-the-art update on integrated CO2 capture and electrochemical conversion systems[J].ChemElectroChem,2022,9(5):e202101540.
- [15]LOBACCARO P,SINGH M R,CLARK E L,et al.Effects of temperature and gas-liquid mass transfer on the operation of small electrochemical cells for the quantitative evaluation of CO2reduction electrocatalysts[J].Physical Chemistry Chemical Physics,2016,18(38):26777-26785.
- [16]LEE G,LI Y C,KIM J Y,et al.Electrochemical upgrade of CO2from amine capture solution[J].Nature Energy,2020,6(1):46-53.
- [17]CHEN L,LI F W,ZHANG Y,et al.Electrochemical reduction of carbon dioxide in a monoethanolamine capture medium[J].ChemSusChem,2017,10(20):4109-4118.
- [18]GASSNER F,LEITNER W.Hydrogenation of carbon dioxide to formic acid using water-soluble rhodium catalyststs[J].Journal of the Chemical Society,Chemical Communications,1993(19):1465.
- [19]GAO N,QUIROZ-ARITA C,DIAZ L A,et al.Intensified co-electrolysis process for syngas production from captured CO2[J].Journal of CO2 Utilization,2021,43:101365.
- [20]邢晨健,王瑞林,赵传文.燃煤电站与光伏余热辅助胺法脱碳系统集成[J].洁净煤技术,2021,27(2):170-179.XING Chenjian,WANG Ruilin,ZHAO Chuanwen.Integration of coal-fired power station and photovoltaic waste heat-assisted amine decarbonization system[J].Clean Coal Technology,2021,27(2):170-179.
- [21]SINGH D,CROISET E,DOUGLAS P L,et al.Techno-economic study of CO2 capture from an existing coal-fired power plant:MEA scrubbing vs.O2/CO2 recycle combustion[J].Energy Conversion and Management,2003,44(19):3073-3091.
- [22]TOWLER G,SINNOTT R.Chemical engineering design:principles,practice and economics of plant and process design[J]2008.
- [23]武文杰.焦炉煤气燃气轮机联合循环电厂系统特性分析与优化设计[D].上海:上海交通大学,2012.
- QIU Dongya
- ZHAO Chuanwen
- JIN Dongling
- GUO Yafei
- School of Energy and Mechanical Engineering
- Nanjing Normal University
- QIU Dongya
- ZHAO Chuanwen
- JIN Dongling
- GUO Yafei
- School of Energy and Mechanical Engineering
- Nanjing Normal University