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A novel technical route based on wet flue gas desulfurization process for flue gas dehumidification, water and heat recovery

机译:基于湿烟气除湿,水和热回收的新型技术路线

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摘要

To recover the water and heat in industrial flue gas before discharging, a novel dehumidification system was proposed by combining the liquid-desiccant-based dehumidification (LDD) method with the existing wet flue gas desulfurization (WFGD) process in a single spraying tower. Calcium chloride (CaCl2) solution was used as a liquid desiccant. A flow pattern controlling (FPC) device was designed to further enhance the mass transfer in the dehumidification process. The effects of liquid-to-gas ratio (L/G), desiccant solution temperature (T-de), desiccant concentration (omega), and superficial flue gas velocity (v(g)) on the dehumidification performance were investigated. The water and heat recovery process of the LDD-WFGD system were analyzed theoretically in detail. Furthermore, the application potential of the proposed LDD-WFGD system for water and heat recovery for coal-fired power plants was discussed by conducing case studies. The recovered water from flue gas could supply 47.2% and 44.8% of the water demand for the WFGD systems in 660 MW and 330 MW power plants, respectively.
机译:为了在排出之前恢复工业烟气中的水和热量,通过将液滴基除湿(LDD)方法与在单个喷涂塔中的现有的湿烟气脱硫(WFGD)方法组合来提出一种新的除湿系统。使用氯化钙(CaCl 2)溶液作为液体干燥剂。设计流动模式控制(FPC)器件以进一步增强除湿过程中的传质。研究了液 - 气体比(L / g),干燥剂溶液温度(T-DE),干燥剂浓度(OMEGA)和浅表烟道气速度(V(g))对除湿性能的影响。理论上详细分析了LDD-WFGD系统的水和热回收过程。此外,通过遏制案例研究讨论了燃煤发电厂水和热回收的所提出的LDD-WFGD系统的应用潜力。来自烟气的回收的水分别为660 MW和330 MW发电厂的WFGD系统供应47.2%和44.8%。

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