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Dynamic simulation of fouling in a circulating fluidized biomass-fired boiler

机译:循环流化床生物质锅炉结垢的动态模拟

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摘要

A dynamic model is presented for a biomass-fired circulating fluidized bed boiler. The model is based on energy and mass balances for the components in the boiler and on a combustion model for the fluidized bed. The main purpose of the model is to simulate how deposits affect the boiler efficiency and performance. The model is verified against the municipal circulating fluidized bed boiler in Vasteras, Sweden, which produces 157 MW. The distribution of deposits on the surfaces in the boiler is well known from inspections. These observations are used as inputs to the model to simulate their effects on boiler performance. The heat exchanger most affected by fouling is Superheater 2, which is the first heat exchanger in the flue gas channel. Deposits typically reduce the heat transfer rate by half over a season despite soot blowing. This and other fouling scenarios are simulated and presented in this article. The simulations show that fouling on superheaters redistributes the heat transfer rate from the superheaters to Reheater 1 and partially redistributes turbine power from the high pressure turbine to the intermediate pressure turbine. If the boiler is running at maximum load, water injection to Reheater 1 has to increase to maintain temperatures below the permitted limit. The dynamic effects of fouling are small and the total efficiency of the boiler is only marginally affected. Fouling on evaporating surfaces has major dynamic effects and dramatically decreases the boiler efficiency. A decrease in fuel rate flow is needed to maintain temperatures in the fluidised bed and in the flue gas channel within acceptable limits.
机译:提出了生物质循环流化床锅炉的动力学模型。该模型基于锅炉中组件的能量和质量平衡,并基于流化床的燃烧模型。该模型的主要目的是模拟沉积物如何影响锅炉的效率和性能。该模型已针对瑞典Vasteras的市政循环流化床锅炉进行了验证,该锅炉的发电量为157 MW。锅炉表面沉积物的分布从检查中是众所周知的。这些观察值用作模型的输入,以模拟它们对锅炉性能的影响。受结垢影响最大的热交换器是过热器2,它是烟气通道中的第一个热交换器。尽管吹灰,沉积物通常会使整个季节的传热率降低一半。本文模拟并介绍了这种污垢情况。仿真显示,过热器上的结垢将热量从过热器重新分配给再热器1,并将涡轮机功率从高压涡轮部分重新分配给中压涡轮。如果锅炉以最大负荷运行,则必须增加向再热器1的注水量,以保持温度低于允许的极限。结垢的动态影响很小,锅炉的总效率仅受到很小的影响。蒸发表面上的污垢具有重大的动态影响,并大大降低锅炉效率。需要降低燃料流量,以将流化床和烟气通道中的温度保持在可接受的范围内。

著录项

  • 来源
    《Applied Energy》 |2011年第5期|p.1813-1824|共12页
  • 作者单位

    Department of Energy Technology, Fluid Dynamics Research Group, Malardalen University, Box 883, SE - 721 23 Vasteras, Sweden;

    Department of Energy Technology, Fluid Dynamics Research Group, Malardalen University, Box 883, SE - 721 23 Vasteras, Sweden,ABB Corporate Research, Department of Automation Technology, Forsgrand 7, SE - 721 78 Vasteras, Sweden;

    Department of Energy Technology, Fluid Dynamics Research Group, Malardalen University, Box 883, SE - 721 23 Vasteras, Sweden;

    Department of Energy Technology, Fluid Dynamics Research Group, Malardalen University, Box 883, SE - 721 23 Vasteras, Sweden;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    dynamic model; cfb boiler; fouling; superheater tubes; deposit layer; biomass-fired boiler;

    机译:动态模型;cfb锅炉;结垢;过热器管;沉积层;生物质锅炉;

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