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1. 国核电力规划设计研究院有限公司
2. 华北电力大学能源动力与机械工程学院
3. 吉林电力股份有限公司
4. 大安吉电绿氢能源有限公司
纸质出版:2025
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杜逸云, 刘路尧, 陈越, 等. 耦合不同制氢技术的合成氨系统技术经济性分析及碳排放评估[J]. 热力发电, 2025,54(5):1-12.
DU Yiyun, LIU Luyao, CHEN Yue, et al. Techno-economic analysis and carbon emission prediction for synthetic ammonia system coupling different hydrogen production technologies[J]. Thermal Power Generation, 2025, 54(5): 1-12.
杜逸云, 刘路尧, 陈越, 等. 耦合不同制氢技术的合成氨系统技术经济性分析及碳排放评估[J]. 热力发电, 2025,54(5):1-12. DOI: 10.19666/j.rlfd.202409218.
DU Yiyun, LIU Luyao, CHEN Yue, et al. Techno-economic analysis and carbon emission prediction for synthetic ammonia system coupling different hydrogen production technologies[J]. Thermal Power Generation, 2025, 54(5): 1-12. DOI: 10.19666/j.rlfd.202409218.
“双碳”背景下,利用可再生电力电解水制氢合成氨,不仅可以消纳可再生能源,解决氢能储运难题,也促进传统合成氨工艺的绿色转型。为了探究不同制氢方案对合成氨系统技术经济性的影响,对比分析了质子交换膜电解槽制氢、质子交换膜电解槽和碱液电解槽制氢比例为1:1以及碱液电解槽制氢3种制氢方案的系统热力性能和经济性能的表现,并利用夹点分析和数学规划相结合的方法,分析了质子交换膜电解槽和碱液电解槽协同制氢合成氨系统的冷热物流集成情况。结果表明:上述3种制氢方案的系统?效率依次为60.3%、56.1%和52.5%,而氨的碳排放也因系统净耗电量的增加而增加;受益于碱液电解槽成熟的制氢工艺,碱液电解槽制氢方案的投资回收期最短,为6.4年,质子交换膜电解槽制氢方案投资回收期最长,达到了12.8年;质子交换膜电解槽和碱液电解槽协同制氢的合成氨系统热集成分析表明,系统中低于100℃的低温余热可经过冷公用工程排向环境;此外,提升电解槽运行温度,有利于改善系统的热力性能,而降低电价、提升系统年运行时长有助于改善系统的经济性。
In the context of “carbon peak” and “carbon neutrality”
using renewable electricity to electrolyze water to produce hydrogen and synthesize ammonia can not only consume renewable energy and solve the problem of hydrogen storage and transportation
but also promote the green transformation of the conventional ammonia synthesis process. To investigate the effect of different hydrogen production schemes on technical and economic performance of the synthetic ammonia system
the system thermal and economic performance of three hydrogen production schemes
including proton exchange membrane electrolyzer hydrogen production
proton exchange membrane electrolyzer and alkaline water electrolyzer hydrogen production in a 1:1 ratio
and alkaline water electrolyzer hydrogen production
are compared and analyzed. The hot and cold integration of the synthetic ammonia system with coordinated hydrogen production by proton exchange membrane electrolyzer and alkaline water electrolyzer is analyzed by combining pinch analysis with mathematical programming. The results show that
the system exergy efficiencies of the above three hydrogen production schemes are 60.3%
56.1% and 52.5%
respectively
and the carbon emissions of ammonia also increase due to the increase in net power consumption of the system. Benefiting from alkaline water electrolyzer's mature hydrogen production process
the alkaline water electrolyzer hydrogen production scheme has the shortest investment payback period of 6.4 years
while the proton exchange membrane electrolyzer hydrogen production scheme has the longest investment payback period of 12.8 years. The thermal integration analysis of the synthetic ammonia system for the coordinated hydrogen production of proton exchange membrane electrolyzer and alkaline water electrolyzer shows that the low-temperature waste heat below 100 ℃ in the system is released to the environment via cold utilities. In addition
increasing the operating temperature of the electrolyzer is beneficial to improving thermal performance of the system
while lowering electricity price and increasing the annual operating hours of the system will help to improve the economic performance of the system.
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