
华南理工大学电力学院
纸质出版:2025
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雷霆, 梁友才, 朱雁, 等. 基于余热回收和液化天然气冷能利用的NGCC电厂燃烧后碳捕集工艺优化[J]. 热力发电, 2025,54(6):194-203.
LEI Ting, LIANG Youcai, ZHU Yan, et al. Process optimization of post-combustion carbon capture for NGCC power plants based on waste heat recovery and liquefied natural gas cold energy utilization[J]. Thermal power generation, 2025, 54(6): 194-203.
雷霆, 梁友才, 朱雁, 等. 基于余热回收和液化天然气冷能利用的NGCC电厂燃烧后碳捕集工艺优化[J]. 热力发电, 2025,54(6):194-203. DOI: 10.19666/j.rlfd.202411229.
LEI Ting, LIANG Youcai, ZHU Yan, et al. Process optimization of post-combustion carbon capture for NGCC power plants based on waste heat recovery and liquefied natural gas cold energy utilization[J]. Thermal power generation, 2025, 54(6): 194-203. DOI: 10.19666/j.rlfd.202411229.
燃烧后碳捕集工艺是实现低碳发电的兜底技术和必然选择,然而其整合至天然气联合循环电厂会大幅降低电厂发电效率。为了降低集成脱碳系统电厂的效率惩罚以及提高整体系统能源利用效率,提出一个综合回收系统余热和液化天然气冷能的新型燃烧后碳捕集流程。首先,对常规碳捕集工艺的关键操作参数包括再生塔压力和贫液载荷进行灵敏度分析得到最佳运行参数,在此基础上开展新型流程的设计及分析。新型流程利用小汽轮机回收低压抽汽的压力,能辅助贫液蒸气压缩并回收CO_2压缩中间冷却热加热再生塔冷凝回流水,在90k Pa的闪蒸压降下每吨CO_2最低再生能耗为3.35GJ,降低了17.3%。此外,通过回收抽汽过热使低压抽蒸汽量从68.40 kg/s降低至48.95 kg/s。针对常规CO_2压缩工艺能耗高和液化天然气气化过程中冷能浪费的问题,提出一种新型CO_2两级压缩中间液化工艺,使压缩功降低了34.5%,并大幅减少冷却负荷和设备数量。?分析结果表明,新型碳捕集工艺和CO_2压缩工艺的?效率分别从23.12%和62.19%升至29.48%和65.96%。模拟结果显示,整合新型碳捕集工艺的发电机组净输出功从341.93 MW增至358.75 MW,净发电效率从48.85%升至51.25%,效率惩罚从13.77%降至9.53%,节能效果十分显著。
Post-combustion carbon capture is the underpinning technology and necessary choice for low-carbon power generation
yet its integration into natural gas combined cycle(NGCC) power plants will significantly reduce the plants' power generation efficiency. In order to reduce the efficiency penalty of the power plants integrated with decarbonization system and improve the energy utilization efficiency of the integrated system
a novel post-combustion carbon capture process that comprehensively recovers the waste heat and liquefied natural gas cold energy is innovatively proposed. Firstly
the key operating parameters of the conventional carbon capture process
including stripper pressure and lean solvent loading
are optimized with sensitivity analysis. On this basis
design and evaluation of novel process is performed. In the novel process
a back-pressure turbine is utilized to recover the pressure energy of the extracted low-pressure steam and assist the lean vapor compression as well as recover the inter-cooling heat of CO_2 compression to heat the reflux condensate of the stripper
which reduces the minimum regeneration energy consumption by 17.3%(to 3.35 GJ) at the flash pressure drop of 90 k Pa.Furthermore
the extracted low-pressure steam is reduced from 68.40 kg/s to 48.95 kg/s by recovering the superheat of steam extraction. Aiming at solving the problems of high energy consumption of the conventional CO_2 compression process and the waste of cold energy in the liquefied natural gas regasification process
a novel CO_2 two-stage compression and intermediate liquefication process is proposed
reducing compression work by 34.5%
and the cooling load and the number of equipment were significantly decreased. Exergy analysis results show that the exergy efficiencies of the novel carbon capture process and CO_2 compression process increase from 23.12% and 62.19% to 29.48% and 65.96%
respectively. The simulation results show that
the net power output of the plant integrated with the novel carbon capture process increases from 341.93 MW to 358.75 MW
resulting in a significant energy saving by increasing the net power output efficiency from 48.85% to 51.25% and decreasing the efficiency penalty from 13.77% to 9.53%.
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