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燃煤机组烟气余热及水回收系统变工况特性和调控策略

Study on Off-design Condition Characteristics and Control Strategy of Fluegas Waste Heat and Water Recovery System of Coal-Fired Power Plants

  • 摘要: 针对燃煤机组烟气余热及水回收系统展开研究,基于物质、能量平衡以及等效热降法分析了系统的节水节煤能力,进而建立了系统变工况分析模型,研究了环境温度和调控策略对系统性能及状态参数的影响规律。结果表明,设计工况下系统节水潜力为15.34 kg/s,节能潜力为2.75 g/(kW·h)。环境温度变化时,系统的部分状态点温度会随着环境温度降低而降低,环境温度为−20℃时,低温省煤器节煤量降至1.44 g/(kW·h)。为避免系统发生低温腐蚀,提出了运行调控策略,使进入电除尘器烟气温度提升至90℃以上,以保证系统的安全运行,但低温省煤器的节煤量相比于未调整时降低了0.2 g/(kW·h)。

     

    Abstract: A fluegas waste heat and water recovery system for the coal-fired power plant is studied in this paper. Based on the material, energy balance and equivalent heat drop method, the water-saving and coal-saving capacity of the system were calculated. Off-design models of the system were developed, influences of environmental temperature and control strategy on system performance and state parameters were evaluated. Results show that the water-saving potential of the system is 15.34 kg/s under the design condition, and the energy-saving potential is 2.75 g/(kW·h). When the ambient temperature changes, the temperature of some state points of the system will decrease with the ambient temperature. The coal saving of the low-temperature economizer will be reduced to 1.44 g/(kW·h) when the ambient temperature is –20°C. To prevent low-temperature corrosion of the system, the operation strategy was proposed, the fluegas temperature entering the electrostatic precipitator is increased to 90°C, which can ensure the safe operation of the system. However, the coal saving of the low-temperature economizer is lower than that of the unadjusted by 0.2 g/(kW·h).

     

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