Thermodynamic evaluation of a Ca-Cu looping post-combustion CO2 capture system integrated with thermochemical recuperation based on steam methane reforming

被引:0
|
作者
He, Song [1 ,2 ,8 ]
Zheng, Yawen [2 ,3 ]
Zeng, Xuelan [1 ,2 ]
Wang, Junyao [4 ,5 ]
Gao, Lifan [1 ,2 ]
Yang, Dongtai [6 ,7 ]
机构
[1] Guangdong Univ Technol, Guangdong Basic Res Ctr Excellence Ecol Secur & Gr, 100 Waihuan Xi Rd, Guangzhou 510006, Peoples R China
[2] Guangdong Univ Technol, Collaborat Innovat Inst Carbon Neutral & Green Dev, 100 Waihuan Xi Rd, Guangzhou 510006, Peoples R China
[3] China Shenzhen Gas Corp Ltd, Shenzhen 518040, Peoples R China
[4] Guangdong Univ Technol, Sch Mat & Energy, Guangzhou 510006, Peoples R China
[5] Guangdong Prov Key Lab Funct Soft Matter, Guangzhou 510006, Peoples R China
[6] Chinese Acad Sci, Inst Engn Thermophys, Lab Integrated Energy Syst & Renewable Energy, Beijing 100190, Peoples R China
[7] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
[8] Cranfield Univ, Sch Water Energy & Environm, Cranfield MK43 0AL, Beds, England
基金
中国国家自然科学基金;
关键词
Calcium looping; Chemical looping combustion; Thermochemical recuperation; Post-combustion CO 2 capture; DISTRIBUTED ENERGY SYSTEM; CARBON-DIOXIDE CAPTURE; GAS COMBINED-CYCLE; HYDROGEN-PRODUCTION; POWER-PLANTS; CALCIUM; COMBUSTION; COAL; PERFORMANCE; TECHNOLOGY;
D O I
10.1016/j.csite.2024.105327
中图分类号
O414.1 [热力学];
学科分类号
摘要
The calcium looping integrated with the chemical looping combustion (CaL-CLC) process is an efficient and cost-effective CO2 capture technology that avoids the energy-intensive air separation unit in the calcium looping (CaL) process. However, in these CaL-CLC and CaL system integration schemes, the carbonation heat is utilized for steam generation, resulting a significant temperature difference and considerable irreversible loss. To prevent temperature mismatch, this paper proposes a novel Ca-Cu looping post-combustion CO2 capture method with thermochemical recuperation based on steam methane reforming. Additionally, a novel system integrated with turbine exhaust heat recovery is introduced to effectively reduce carbon emissions from flue gas. Results show that the proposed system has superior performance compared to the reference system based on the Ca-Cu looping method. The specific primary energy consumption for CO2 avoidance decreased from 2.40 MJLHV/kg CO2 in the reference system to 2.02 MJLHV/kg CO2. Exergy analysis indicates that a total of 3.0 % reduction in exergy destruction can be achieved in chemical reaction processes and heat recovery processes, contributing to the superior performance of the proposed system. Furthermore, the effects of key operating parameters indicate that cascaded turbine exhaust recovery is essential for improving the thermodynamic efficiency of the proposed system. Overall, recovering the mid-temperature carbonation heat via thermochemical regeneration and integrating with exhaust heat recovery contribute to reducing SPECCA, thus providing a promising low-energy-consumption alternative for CO2 capture.
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页数:15
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