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Chemkin simulation of mercury oxidation in a condensing heat exchanger.

机译:冷凝热交换器中汞氧化的Chemkin模拟。

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摘要

Mercury oxidation in a slip stream condensing heat exchanger (CHX) developed by the Energy Research Center (ERC) at Lehigh University was modeled using hundreds of possible chemical reactions and tens of species in coal-fired power plant furnace and flue gas downstream of the furnace. The modeling tools, CHEMKIN, SENKIN and PSR were used to conduct equilibrium calculations in the furnace and the kinetic calculations in the flue gas leading to the CHX. The detailed mechanism of mercury speciation at the furnace and downstream of the furnace has been investigated. Atomic chlorine is generated in the furnace and flows downstream of furnace, where it reacts with elemental mercury (Hg 0). The predicted results suggest oxidation of Hg0 in the CHX occurs by this mechanism. Performance tests of the CHX at Great River Energy's Coal Creek Station were carried out to study moisture, mercury and acid capture abilities of the CHX. The elemental mercury reduction rate and the amount of condensed water were measured in these tests. The measured results show ~35% of Hg0 was oxidized in the CHX. The mercury oxidation results show agreement between simulation and test within a typical range of HCl concentration of flue gas at furnace exit from 20 ppmv to 50 ppmv. The kinetic calculations downstream of the furnace show the oxidation reaction between Hg0 and atomic Cl primarily occurs at temperature 600K to 300K. The flue gas temperature in the CHX affects condensed water formation and mercury oxidation rate. An analytical model of heat and mass transfer processes in the CHX was used to obtain predictions of flue gas temperature profiles with different CHX inlet cooling water temperatures. The simulation results with lower CHX inlet cooling water temperature, which leads to higher flue gas cooling rate and reduced flue gas moisture content in the CHX, suggest higher Hg0 oxidation rates would be obtained. The predicted Hg 0 reduction rate in the CHX increased to ~42% with CHX inlet cooling water temperature of 35°F and a HCl concentration at the furnace exit of 40 ppmv.
机译:由利哈伊大学能源研究中心(ERC)开发的滑流冷凝式热交换器(CHX)中的汞氧化是使用燃煤电厂炉中的数百种可能的化学反应和数十种物质以及炉下游的烟道气进行建模的。使用建模工具CHEMKIN,SENKIN和PSR在炉中进行平衡计算,并对通向CHX的烟道气进行动力学计算。研究了炉子和炉子下游汞形态的详细机理。原子氯在熔炉中产生,并在熔炉下游流动,并与元素汞(Hg 0)反应。预测结果表明,CHX中Hg0的氧化是通过这种机制发生的。在大河能源的煤溪站进行了CHX的性能测试,以研究CHX的水分,汞和酸捕获能力。在这些测试中测量了元素汞还原速率和冷凝水量。测量结果表明,约35%的Hg0在CHX中被氧化。在炉出口处烟气的HCl浓度范围从20 ppmv到50 ppmv的典型范围内,汞的氧化结果表明模拟和测试之间是一致的。炉子下游的动力学计算表明Hg0和原子Cl之间的氧化反应主要发生在600K至300K的温度下。 CHX中的烟气温度会影响冷凝水的形成和汞的氧化速率。 CHX中传热和传质过程的分析模型用于获得不同CHX入口冷却水温度下的烟道气温度曲线预测。较低的CHX入口冷却水温度的模拟结果可导致较高的烟道气冷却速率并降低CHX中的烟道气水分含量,表明将获得较高的Hg0氧化率。在CHX入口冷却水温度为35°F,炉膛出口处的HCl浓度为40 ppmv的情况下,CHX中的Hg 0预测还原率增加至〜42%。

著录项

  • 作者

    Wang, Xingchao.;

  • 作者单位

    Lehigh University.;

  • 授予单位 Lehigh University.;
  • 学科 Engineering Mechanical.
  • 学位 M.S.
  • 年度 2014
  • 页码 61 p.
  • 总页数 61
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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