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Flue gas desulfurization and humidification dehumidification in power plants

机译:电厂烟气脱硫加湿除湿

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摘要

Performance evaluation is presented for flue gas desulfurization (FGD), humidification and dehumidification desalination (HDD) of flue gases emitted from power plants. The proposed system is based on use of seawater for SO_2 absorption and removal from the flue gases. The FGD and HDD processes are separated in order to achieve the highest possible efficiency. This is because FGD requires low temperatures to achieve high rates of absorption and removal of SO_2. On the other hand, HDD requires higher temperatures to provide sufficient temperature difference and driving force for humidification and dehumidification. Analysis of both systems is applied to the emission rate data of power plants in Kuwait. The design results of the seawater SO_2 absorption column showed variations in the column height between 8.1-12.6 m as the power plant capacity was increased from 244-4173 MW. Analysis of the HDD system show that it might not be the optimum desalination alternative because of its limited production capacity. However, the process layout is simple and can be formed of two packed columns for humidification and dehumidification, which requires a small capital when compared to conventional thermal or membrane desalination.
机译:提出了对电厂排放的烟道气脱硫(FGD),加湿和除湿脱盐(HDD)的性能评估。拟议的系统基于使用海水吸收和去除烟道气中的SO_2。 FGD和HDD流程分开,以实现最高的效率。这是因为FGD需要低温才能实现SO_2的高吸收率和去除率。另一方面,HDD需要更高的温度以提供足够的温度差和用于加湿和除湿的驱动力。对这两个系统的分析都应用于科威特发电厂的排放率数据。海水SO_2吸收塔的设计结果表明,随着电厂容量从244-4173 MW增加,塔高在8.1-12.6 m之间变化。对HDD系统的分析表明,由于其生产能力有限,它可能不是最佳的脱盐替代方案。但是,该工艺布置简单,并且可以由两个用于加湿和除湿的填充塔形成,与常规的热脱盐或膜脱盐相比,这需要很少的资金。

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