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Cool SCRs Come to America Next Generation SCR Choices - High-Dust, Low-Dust and Tail-End

机译:很酷的scrs来到美国下一代SCR选择 - 高尘,低尘和尾端

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The great majority SCR installations in the US power plants are of the High dust (high temperature) type, treating the flue gas exiting the economizer. European experience includes two more variations of SCRs: Low-Dust version that treats flue gas after the particulate collection device, and Tail-End version, which treats the saturated flue gas exiting a wet FGD absorber. Retrofitting coal units with high dust SCRs is getting increasingly problematic; the easy installations have been already retrofitted. Going forward, utilities are seriously considering low dust and tail-end locations when the high-dust alternative is considered impractical. The most significant aspect of low dust and tail-end SCRs is the requirement for reheating the flue gas to 550- 650°F, then recuperating the heat energy by cooling the gas back to about 250-350°F. This type of heat exchanger is termed Gas-to-Gas Heater, GGH in short. The most common heat exchangers used are the regenerative (Ljungstrom) type; although zero leakage tubular types may be considered, depending mostly on capital cost. Both heating alternatives require additional heat input, via steam coil or fired natural gas, to provide the differential temperature rise from the GGH exit to the needed temperature for effective catalyst operation. Tail end installations have certain advantages regarding the catalyst type: less volume, longer life span and lower cost, as compared to both high and low dust. On the other hand, flue gas reheat energy for the Tail-End SCR normally present a significant penalty, which is higher than the Low-Dust heating requirement. In comparison, High-Dust SCR configuration requires no supplemental heating at high loads. This paper investigates power plant conditions that would exclude high dust SCRs and favor Low-Dust or Tail-End, describes the design characteristics of both types and summarizes European experience. In addition, the paper presents an economic evaluation of the Low-Dust and Tail-End SCR installations.
机译:美国发电厂的大多数SCR设施都是高粉尘(高温)类型,处理离开节能器的烟气。欧洲经验包括两种SCR的变化:低粉尘版本,可在颗粒收集装置后处理烟气,以及尾端版本,其处理离开湿FGD吸收器的饱和烟道气。用高尘埃克拉的改造煤装置越来越有问题;易于安装已经改装。前进,当高尘替代方案被认为是不切实际的时,公用事业公司正在考虑低灰尘和尾端位置。低灰尘和尾端SCR最重要的方面是要求将烟道气再加热至550-650°F,然后通过将气体冷却至约250-350°F来恢复热能。这种类型的热交换器被称为气流加热器,简称GGH。使用的最常见的热交换器是再生(Ljungstrom)类型;尽管可以考虑零泄漏管类型,这主要取决于资本成本。两种加热替代方案都需要额外的热输入,通过蒸汽线圈或烧制的天然气,以提供从GGH出口到所需温度的差分温度升高,以进行有效的催化剂操作。与高灰尘相比,尾部安装有关催化剂类型的某些优点:较少的体积,寿命更少,寿命较长,成本更低。另一方面,尾端SCR的烟气再加热能量通常呈现出显着的罚款,其高于低粉尘加热要求。相比之下,高尘埃SCR配置不需要在高负荷下加热。本文调查了排除高粉尘SCR的电厂条件,并有利于低粉尘或尾端,描述了两种类型的设计特征,总结了欧洲经验。此外,本文提出了对低粉尘和尾端的SCR装置的经济评估。

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