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基于热力学第二定律的化学吸收法碳捕集系统能效分析

Energy Efficiency Analysis of Carbon Capture Systems Using Chemical Absorption Based on the Second Law of Thermodynamics

  • 摘要:
      目的  文章旨在研究燃煤烟气化学吸收法碳捕集系统的实际能效,为该技术的优化与推广提供科学依据。
      方法  首先,梳理了国内外典型化学吸收法碳捕集系统的能耗现状,明确了现有技术的能耗水平。随后,基于实际工程案例,对化学吸收法碳捕集系统进行了热平衡分析,并测试计算了系统的热耗与电耗。在此基础上,提出了等效总能耗的计算方法,以更全面地评估系统的综合能耗,并引入“热力学第二定律效率”的热经济学评价方法,对系统能效进行了剖析。进一步地,以系统中关键的耗能环节−蒸汽热耗为例,开展了㶲损失分析,揭示了能量利用的关键节点。
      结果  结果表明,目标碳捕集系统的等效总电耗为397.8 kWh/t CO2,等效总热耗为33.4 GJ/t CO2,热力学第二定律效率达到28.1%,蒸汽㶲损失率为18.81%。与现有化学吸收法碳捕集技术相比,该系统在能耗控制与能量利用效率方面较优,但仍存在进一步优化的空间。
      结论  建议进一步对碳捕集系统进行吸收剂研究和过程工艺优化,提升系统热力学第二定律效率,探索更经济的热源替代方案,或利用热泵技术回收蒸汽疏水中的低品位余热、实现能源的循环利用,从而降低高品位能源的消耗,提升系统的整体经济性。

     

    Abstract:
      Objective  This study aims to investigate the actual energy efficiency of coal-fired flue gas chemical absorption-based carbon capture systems, providing a scientific basis for the optimization and promotion of this technology.
      Method  Initially, the energy consumption status of typical chemical absorption-based carbon capture systems worldwide was reviewed to establish the energy consumption levels of existing technologies. Subsequently, based on actual engineering cases, a heat balance analysis of the chemical absorption-based carbon capture system was conducted, and the system's heat and electricity consumption were measured and calculated. On this foundation, an equivalent total energy consumption calculation method was proposed to comprehensively evaluate the system's overall energy consumption. The concept of "Second Law of Thermodynamics efficiency" was introduced as a thermo-economic evaluation method to analyze the system's energy efficiency. Furthermore, by taking the steam thermal consumption - one of the critical energy-consuming links in the system - as an example, an exergy loss analysis was performed to identify critical nodes of energy utilization.
      Result  The results indicate that the target carbon capture system has an equivalent total electricity consumption of 397.8 kWh/t CO2, an equivalent total heat consumption of 33.4 GJ/t CO2, a Second Law of Thermodynamics efficiency of 28.1%, and a steam exergy loss rate of 18.81%. Compared with existing chemical absorption-based carbon capture technologies, the system demonstrates superior performance in energy consumption control and energy utilization efficiency, although further optimization potential remains.
      Conclusion  It is recommended to conduct further research on absorbents and optimize the process technology for the carbon capture system to enhance the system's Second Law of Thermodynamics efficiency. Exploring more economical heat source alternatives or utilizing heat pump technology to recover low-grade heat from steam condensate for energy recycling could reduce the consumption of high-grade energy and improve the system's overall economic viability.

     

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