Comprehensive evaluation of various CO2 capture technologies through rigorous simulation: Economic, equipment footprint, and environmental analysis

被引:4
作者
Chang, Shou-Feng [1 ]
Chiu, Hsuan-Han [2 ]
Jao, Han-Shu [1 ]
Shang, Jin [3 ]
Lin, Yu-Jeng [4 ]
Yu, Bor-Yih [1 ]
机构
[1] Natl Taiwan Univ, Dept Chem Engn, Taipei, Taiwan
[2] Purdue Univ, Davidson Sch Chem Engn, 480 West Stadium Ave, W Lafayette, IN USA
[3] City Univ Hong Kong, Sch Energy & Environm, Hong Kong, Peoples R China
[4] Natl Tsing Hua Univ, Dept Chem Engn, Hsinchu, Taiwan
来源
CARBON CAPTURE SCIENCE & TECHNOLOGY | 2025年 / 14卷
关键词
CO2; capture; Absorption; Adsorption; Economics; Footprint; SWING ADSORPTION; CARBON-DIOXIDE; FLUE-GAS; OPTIMIZATION; DESIGN; BIOGAS;
D O I
10.1016/j.ccst.2024.100342
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The comprehensive evaluation of various CO2 capture technologies from multiple perspectives remains limited, yet it is crucial for the successful implementation and deployment of carbon capture solutions to achieve carbon neutrality. This study presents a framework for assessing representative CO2 capture processes from key point sources through rigorous simulation. Eight scenarios were developed and compared, comprising four standalone processes ( i.e. , physical absorption (PHYABS), chemical absorption (CHEABS), dual-reflux pressure swing adsorption (DRPSA) and pressure-temperature swing adsorption (PTSA)) and four hybrid processes that integrate different adsorption and absorption processes. To evaluate each scenario, an integrated indicator, the Economics, Equipment footprint, and Environmental Score (EEES), was introduced. Our results indicate that the standalone CHEABS exhibits the lowest EEES of 0.120, highlighting its technological readiness and superiority over other processes. In contrast, the standalone PHYABS (EEES = 0.168) and the hybrid PHYABS/PTSA process (EEES = 0.242) emerge as viable alternatives, balancing environmental performance with economic and spatial considerations. Standalone PTSA (EEES = 0.465) and DRPSA (EEES = 0.706) are less favorable because of their higher utility demands and larger equipment footprints. Similarly, hybrid processes, namely, DRPSA/CHEABS (EEES = 0.891), CHEABS/PTSA (EEES = 0.837), and DRPSA/PHYABS (EEES = 0.784), are less advantageous across all three metrics. Furthermore, sensitivity analyses indicated that carbon permit prices exert a negligible effect on the process economics. Additionally, it appears that government subsidies may play a crucial role in facilitating the development of CO2 capture technologies within the industrial sector. Overall, this study provides a robust framework for evaluating CO2 capture processes and offers practical recommendations for technology deployment.
引用
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页数:19
相关论文
共 74 条
[1]  
[Anonymous], 2019, Transforming Industry through CCUS, DOI [10.1787/09689323-en, DOI 10.1787/09689323-EN]
[2]  
AspenTech, Rate-Based Model of the CO2 Capture Process by MEA using Aspen Plus
[3]   Zeolites as Selective Adsorbents for CO2 Separation [J].
Boer, Dina G. ;
Langerak, Jort ;
Pescarmona, Paolo P. .
ACS APPLIED ENERGY MATERIALS, 2023, 6 (05) :2634-2656
[4]   Direct Air Capture of CO2: A Key Technology for Ambitious Climate Change Mitigation [J].
Breyer, Christian ;
Fasihi, Mahdi ;
Bajamundi, Cyril ;
Creutzig, Felix .
JOULE, 2019, 3 (09) :2053-2057
[5]   A review of degradation and emissions in post-combustion CO2 capture pilot plants [J].
Buvik, Vanja ;
Hoisaeter, Karen K. ;
Vevelstad, Sorun J. ;
Knuutila, Hanna K. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2021, 106
[6]  
Chakravarti S., 2001, 1 NAT C CARB SEQ CIT
[7]   Evaluation of alternative processes of methanol production from CO2: Design, optimization, control, techno-economic, and environmental analysis [J].
Chiou, Hsuan-Han ;
Lee, Chi-Jui ;
Wen, Bo-Sheng ;
Lin, Jian-Xun ;
Chen, Cheng-Liang ;
Yu, Bor-Yih .
FUEL, 2023, 343
[8]   Synthesis of green light olefins from direct hydrogenation of CO2. Part I: Techno-economic, decarbonization, and sustainability analyses based on rigorous simulation [J].
Chiu, Hsuan-Han ;
Yu, Bor-Yih .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2024, 156
[9]   Synthesis of green light olefins from direct hydrogenation of CO2. Part II: detailed process design and optimization [J].
Chiu, Hsuan-Han ;
Yu, Bor-Yih .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2024, 155
[10]   Hybrid modeling of vacuum swing adsorption carbon capture process for rapid process-level evaluation of adsorbents [J].
Chung, Wonsuk ;
Kim, Jukbin ;
Jung, Howoun ;
Lee, Jay H. .
CHEMICAL ENGINEERING JOURNAL, 2024, 495