1. 福州大学电气工程与自动化学院
2. 中国科学院福建物质结构研究所泉州装备制造研究中心
3. 中国科学院大学福建学院
4. 厦门大学能源学院
5. 中南大学能源科学与工程学院
纸质出版:2026
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魏蝶, 张留淦, 林健, 等. 寒冷地区压缩气体供热与水基碳捕集耦合系统研究[J]. 热力发电, 2026,(9).
魏蝶, 张留淦, 林健, et al. 寒冷地区压缩气体供热与水基碳捕集耦合系统研究[J]. Thermal Power Generation, 2026, (9).
魏蝶, 张留淦, 林健, 等. 寒冷地区压缩气体供热与水基碳捕集耦合系统研究[J]. 热力发电, 2026,(9). DOI: 10.19666/j.rlfd.202512034.
魏蝶, 张留淦, 林健, et al. 寒冷地区压缩气体供热与水基碳捕集耦合系统研究[J]. Thermal Power Generation, 2026, (9). DOI: 10.19666/j.rlfd.202512034.
【目的】为解决寒冷地区冬季供暖面临的高碳排放和清洁供暖需求间的矛盾,突破传统水基碳捕集法在常压下CO
2
溶解度受限的技术瓶颈,本文提出了一种寒冷地区压缩气体供热与水基碳捕集耦合系统。【方法】系统集成了气体压缩、水基碳捕集和余热回收技术,利用寒冷地区天然冷能优势,降低气体压缩能耗的同时提升CO
2
溶解能力,并回收压缩热用于供暖,实现碳捕集与清洁供暖的协同增效。基于热力学仿真建模,对系统的捕集性能、能耗特性及供热能力进行了多维度的量化分析。【结果】结果表明:在10 MW供热负荷工况下,系统的CO
2
捕集能耗仅为290.18 kW·h/t,对应能耗成本为183.51元/t,较传统胺基化学吸收法降低约25.43%;敏感性分析进一步表明,系统在较低环境温度、二级吸收压力≥1 200 kPa、二级循环水流量约300~500 kg/s以及入口CO
2
浓度≥15%的工况下运行性能更优。【结论】本研究提出的耦合系统通过压缩热梯级利用和两级碳捕集循环的协同设计,实现了高效碳捕集和稳定供暖,为寒冷地区实现清洁供暖与碳减排目标提供了一种新思路。
[Objective
]
To address the practical challenges in cold northern regions of China
including the growing demand for winter heating
severe pollution from coal combustion
and the performance degradation
efficiency drop and frost formation of air-source heat pumps under low-temperature conditions
this paper proposes a novel compressed gas heating and water-based carbon capture integrated system. [Methods
]
The system increases the pressure of flue gas through multi-stage compression
with the compression heat being utilized in a cascaded manner. The high-grade compression heat is used for residential heating
thereby avoiding the problem of frost formation in low-temperature environments with heat pump heating. Subsequently
the low-grade compression heat is harnessed to preheat the gas before it enters the expander within the expansion module
thus increasing the power output of the expander. In parallel
a t
wo-stage water-based carbon absorption-desorption cycle is adopted to achieve CO
2
enrichment and purification
harnessing the cold climate of northern regions to promote the dissolution of CO
2
into the circulating water
while recovering a portion of the compression work via the expander. To evaluate the system's performance
a simulation model of the proposed system is constructed in Aspen Plus
with the specific energy consumption for CO
2
capture
heating load
CO
2
separation efficiency
and product gas purity designated as the key performance indicators. Based on these criteria
a quantitative performance analysis of the system is then carried out. A sensitivity study is conducted on key parameters such as ambient temperature and absorption pressure. [Results
]
Under the design condition of 10 MW heating supply
the system achieves a CO
2
capture rate of 85.65% and a product gas purity of 99.72%. The specific energy consumption for CO
2
capture is 290.18 kW·h/t and the capture cost amounts to 183.51 yuan/t
representing a reduction of about 25.43% compared with that of the conventional amine-based capture technology. Sensitivity analysis indicates that lower ambient temperature
higher second-stage absorption pressure(≥1 200 kPa)
a moderate second-stage circulating water flow rate(300~500 kg/s)
and a medium-to-high inlet CO
2
concentration(≥15%) are conducive to achieving low-energy and high-efficiency operation of the system. [Conclusion
]
This study proposes an integrated system that combines compressed gas heating
low-temperature water-based carbon capture
and cascaded waste heat utilization
which enables the effective synergistic achievement of the dual goals of heating supply and carbon emission reduction. The system features the advantages of low capture energy consumption
stable heat supply
and strong environmental adaptability
providing a promising technical pathway for clean heating and low-carbon flue gas treatment in col
d northern regions.
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