
东南大学 能源与环境学院,江苏,南京,210096
Published Online:15 March 2025,
Published:2025
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罗启炜,向文国. 基于叠式流化床的钙循环生物质气化制氢经济性动力工程学报, 2025, 45(3): 464-473 https://doi.
org/10.19805/j.cnki.jcspe.2025.240155
罗启炜,向文国. 基于叠式流化床的钙循环生物质气化制氢经济性动力工程学报, 2025, 45(3): 464-473 https://doi. DOI: 10.19805/j.cnki.jcspe.2025.240155.
org/10.19805/j.cnki.jcspe.2025.240155 DOI:
以叠式流化床作为钙循环生物质气化炉
探索了钙循环生物质气化制氢协同捕获CO
2
实现负碳排放的技术经济性。建立了零碳排放和负碳排放生物质气化制氢系统的模型
对2个系统进行了模拟研究
并进行了经济性能分析。结果表明:叠式流化床气化炉的制氢平准成本(LCOH)在零碳排放工况下为2.78 美元/kg
在负碳排放工况下为2.93 美元/kg
在考虑CO
2
销售收入情况下
负碳排放下LCOH可进一步降低至2.47 美元/kg;基于叠式流化床气化炉的负碳排放生物质制氢系统不仅成本更低
而且表现出卓越的碳减排潜力。
Using compact fluidized bed as calcium cycle biomass gasifier to explore the techo-economic feasibility of synergistic capture of CO
2
and hydrogen production through calcium cycle biomass gasification
thereby achieving negative carbon emissions. Models for zero carbon and negative carbon biomass gasification hydrogen production systems were established
simulation on both systems was conducted
and analysis of economic performance was conducted. Results show that the levelized cost of hydrogen (LCOH) of the compact fluidized bed gasifier is 2.78 and 2.93 $/kg under zero carbon and negative carbon emission conditions
respectively. Considering the CO
2
market price
LCOH under negativ
e carbon emission condition can be further reduced to 2.47 $/kg. The negative carbon emission biomass hydrogen production system based on compact fluidized bed gasifier not only has lower cost
but also exhibits superior carbon emission reduction potential.
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