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钙循环捕集CO2小试和中试台架研究进展

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燃煤电厂产生CO2会加重温室效应,因此实现温室气体减排目标至关重要.碳捕集技术已被确定为降低电力部门碳排放的关键措施.胺洗涤等化学吸附剂和氧燃烧技术等成熟技术集成到发电厂时,效率损失很高(8.0%~12.5%),因此,为尽量减少效率损失和相关电力成本,需开发新的二氧化碳捕获技术.钙循环工艺是一项很有前途的技术,效率损失可降至7%.由于资金成本高,目前尚未开发出有商业规模的成本效益技术,而在设计和建造商业规模装置前,需深入了解各操作条件的系统行为,以优化工艺参数并评估可行性.概述了全球可用的小试试验台架和中试工厂测试设施,总结了测试设备的特性和操作条件及提取关键的试验结果,表明CaL工艺的可行性在1 kWth~1.9MWth的实验室规模和中试规模设施中得到广泛研究.在这些CaL系统中,碳酸化炉的工作温度600~700 aC,煅烧炉的工作温度800~1 000℃.进入到碳酸化炉里CO2均来自电厂,均可实现90%以上CO2捕集效率.此外,调整操作设计参数,如CO2入口浓度、碳酸化炉或煅烧炉温度等,将影响CO2捕集效率.总之,这些结果为未来大规模台架的开发收集有价值的操作数据,这也将是在未来能源发展中扩大和部署这项技术的关键所在.
Review of bench and pilot-scale testing for calcium looping capture of carbon dioxide
CO2 generated by coal-fired power plants could exacerbate the greenhouse effect,so achieving greenhouse gas emission reduc-tion goals is crucial.Carbon capture technology has been identified as a key measure to reduce carbon emissions in the power sector.When mature technologies such as amine scrubbing and oxygen combustion technology are integrated into power plants,efficiency penal-ty could result in high efficiency penalty(8.0%-12.5%).For this reason,to minimize efficiency penalties and related increased power costs,new carbon dioxide capture technologies have been developed.The calcium looping process is a promising technology that could reduce efficiency penalty to 7%.Due to the high cost of capital,cost-effective technologies with commercial scale have not yet been developed.Before designing and constructing commercial scale devices,it is necessary to have a deep understanding of the system behavior under various operating conditions to optimize process parameters and evaluate feasibility.An overview of the available bench-scale and pilot-scale testing facilities worldwide.Characteristics and operating conditions of the testing equipment were summarized,key experimental results were also extracted,indicating that the feasibility of the CaL process has been widely studied in bench-scale and pi-lot-scale facilities ranging from 1 kWth-1.9 MWth.In these CaL systems,the operating temperature range of the carbonator is 600-700 ℃,and the operating temperature of the calciner is 800-1 000 ℃.The CO2 entering the carbonator comes from the power plant and can achieve CO2 capture efficiency of over 90%.In addition,adjusting operational design parameters such as CO2 inlet concentration,carbonation or calcination temperature,etc.will affect CO2 capture efficiency.In summary,these results provide valuable operational data for the development of future large-scale platforms,which will also be the key to expanding and deploying this technology in future development.

coal fired power plantcarbon capturecalcium loopingbenchpilot plant

王长清、谭煜幺、林明玮、刘文强、邓黎丹、周子健、徐明厚

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华中科技大学煤燃烧与低碳利用国家重点实验室,湖北武汉 430074

燃煤电厂 碳捕集 钙循环 台架 中试工厂

国家自然科学基金青年科学基金资助项目

51906078

2024

洁净煤技术
煤炭科学研究总院 煤炭工业洁净煤工程技术研究中心

洁净煤技术

CSTPCD北大核心
影响因子:0.893
ISSN:1006-6772
年,卷(期):2024.30(8)