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烟气脱硫吸收塔反应过程的数值模拟及试验研究 被引量:26

Numerical Simulation and Experimental Study on Desulfurization Process in FGD Absorbers
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摘要 以鼓泡式脱硫塔为例,采用双膜模型对烟气脱硫过程进行了数值模拟,并与试验结果进行了比较。结果表明:影响鼓泡式脱硫反应过程的主要因素有烟气中SO2含量、吸收液浓度、气体温度、pH值及喷管浸入深度等;在运行中应保持pH值>8和浸管深度>200mm,且吸收液浓度4.5%左右较为合适.同时,脱硫效率对入口烟气温度变化敏感,入口烟气温度越低,脱硫效率越高.通过对这些因素的分析,有助于脱硫装置的运行优化. Taking the bubbling desulferization absorber as an example, numerical simulation on flue gas desulfurization (FGD) process was carried out with a double films model, and the results of which were compared with actual experimental data. Results show that, major factors influencing the bubbling desulfurization process include the SO2 concentration in flue gas, the absorbent concentration, the gas temperature, the pH value and the immersion depth of nozzle etc. It's found to be appropriate in operation that the pH value and immersion depth of nozzle are separately kept to be above 8 and 200mm, and the concentration of adsorbent about 4. 5%. Inlet gas temperature has a significant influence on the desulfurization efficiency, which increases with decreasing inlet gas temperature. Operation optimization of desulfurization equipments is being promoted through above analysis.
出处 《动力工程》 EI CSCD 北大核心 2008年第3期433-437,446,共6页 Power Engineering
关键词 环境科学 数值模拟 烟气脱硫 吸收塔 脱硫效率 environmental science numerical simulation FGD absorber desulfurization efficiency
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  • 1Dantuluri S R, Davis W T, Counce R M, Reed G D.Mathematical model of sulfur dioxide absorption into a calcium hydroxide slurry in a spray dryer [J]. Separation Science and Technology, 1990(25): 1843 ~ 1855.
  • 2Newton GH, Kramlich J, Payne R. Modeling the SO2Slurry droplet reaction [ J]. AICHE Journal, 1990, 36(12): 1865 ~ 1872.
  • 3Scala F, D' Ascenzo M. Absorption with instantaneous reaction in a droplet with sparingly soluble fines [ J ].AICHE. Journal, 2002, 48 (8): 1719~ 1726.
  • 4Zhou, LX. Theory and numerical modeling of turbulent gasparticle flows and combustion [ M ]. Boca Raton: Science Press/CRC Press, 1993.
  • 5Abramzon B, Sirignano A. Droplet vaporization model for spray combustion calculations [ J ]. International journal of heat and mass transfer. 1989, 32(9): 1605 ~ 1618.
  • 6Liang H, Shinohara K, Minoshima H, Matsushima, K.Analysis of constant rate period of spray drying of slurry [J]. Chemical Engineering Science, 2001(56): 2205 ~2213.
  • 7Wang J. Advances in spray drying desulfurization for high sulfur coal [ D ]. Cincinnati: The University of Cincinnati, 1995.
  • 8Babu DR, Narsimhan G, Phillips CR. Absorption of sulfur dioxide in calcium hydroxide solutions [ J ]. Ind. Eng.Chem. Fund, 1984(23): 370~377.
  • 9Ollero P, Salvador L, Ca, adas L. An experimental study of flue gas desulfurization in a pilot spray dryer [ J ].Environmental Progress, 1997, 16 ( 1 ): 20 ~ 28.
  • 10Srivastava RK, Jozewicz W, Singer C. SO2 scrubber technologies: a review [ J ] . Environmental Progress,2001, 20(4): 219 ~ 227.

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