流化床煤燃烧的超临界CO2动力循环热力学分析

IF 1.5 Q3 ENGINEERING, CHEMICAL Journal of Combustion Pub Date : 2018-07-24 DOI:10.1155/2018/6963292
Chenchen Geng, Yingjuan Shao, Wenqi Zhong, Xuejiao Liu
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引用次数: 21

摘要

闭式超临界二氧化碳(S-CO2)布雷顿循环在同等涡轮进口条件下具有更高的循环效率,是一种很有前途的蒸汽朗肯循环替代方案,已被探索应用于核能、太阳能发电、余热回收和燃煤电厂。本研究建立了基于改进再压缩布雷顿循环与燃煤循环流化床(CFB)锅炉集成的300MW S-CO2动力系统。详细研究了两级分流对系统性能的影响。此外,还对关键运行参数进行了热力学分析,包括末端温差、涡轮进口压力/温度、再热级、参数以及压缩机进口压力/温度。结果表明:合理分配再压缩器(SR1)的分流比可获得最大的循环效率,低温回热器(LTR)两侧热容量实现良好匹配。由于LTR比热差逐渐缩小,最佳SR1与高压汽轮机(HPT)进口压力呈近似线性比例减小,循环流化床锅炉省煤器的二次分流比(SR2)可以回收由于温度范围窄而产生的适度烟气热量,提高锅炉效率。终端温差越小,效率越高,回热器的成本和压降也越大,反过来可能会降低效率。在600°C/600°C/25Mpa条件下,单次再热循环效率提高1.5%,而双次再热与蒸汽朗肯循环相比效率提高不明显,主要原因是压力比低得多。再热压力和主压缩机(MC)进口压力有相应的最优值。高压涡轮和低压涡轮进口温度对系统性能都有积极的影响。
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Thermodynamic Analysis of Supercritical CO2 Power Cycle with Fluidized Bed Coal Combustion
Closed supercritical carbon dioxide (S-CO2) Brayton cycle is a promising alternative to steam Rankine cycle due to higher cycle efficiency at equivalent turbine inlet conditions, which has been explored to apply to nuclear, solar power, waste heat recovery, and coal-fired power plant. This study establishes 300MW S-CO2 power system based on modified recompression Brayton cycle integrated with coal-fired circulating fluidized bed (CFB) boiler. The influences of two stages split flow on system performance have been investigated in detail. In addition, thermodynamic analysis of critical operating parameters has been carried out, including terminal temperature difference, turbine inlet pressure/temperature, reheat stages, and parameters as well as compressor inlet pressure/temperature. The results show that rational distribution of split ratio to the recompressor (SR1) achieves maximal cycle efficiency where heat capacities of both sides in the low temperature recuperator (LTR) realize an excellent matching. The optimal SR1 decreases in the approximately linear proportion to high pressure turbine (HPT) inlet pressure due to gradually narrowing specific heat differences in the LTR. Secondary split ratio to the economizer of CFB boiler (SR2) can recover moderate flue gas heat caused by narrow temperature range and improve boiler efficiency. Smaller terminal temperature difference corresponds to higher efficiency and brings about larger cost and pressure drops of the recuperators, which probably decrease efficiency conversely. Single reheat improves cycle efficiency by 1.5% under the condition of 600°C/600°C/25Mpa while efficiency improvement for double reheat is less obvious compared to steam Rankine cycle largely due to much lower pressure ratio. Reheat pressure and main compressor (MC) inlet pressure have corresponding optimal values. HPT and low pressure turbine (LPT) inlet temperature both have positive influences on system performance.
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来源期刊
Journal of Combustion
Journal of Combustion ENGINEERING, CHEMICAL-
CiteScore
2.00
自引率
28.60%
发文量
8
审稿时长
20 weeks
期刊最新文献
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