化工学报 ›› 2014, Vol. 65 ›› Issue (2): 430-436.DOI: 10.3969/j.issn.0438-1157.2014.02.009

• 流体力学与传递现象 • 上一篇    下一篇

螺旋板换热器轴向错流通道湿法捕尘拟均相模型

徐其鹏, 桂月明, 朱家骅, 程远贵, 夏素兰   

  1. 四川大学化工学院, 四川 成都 610065
  • 收稿日期:2013-04-15 修回日期:2013-06-03 出版日期:2014-02-05 发布日期:2014-02-05
  • 通讯作者: 朱家骅
  • 基金资助:

    国家自然科学基金项目(21276161);中央高校基本科研专项(2010SCU22008)。

Pseudo-homogeneous model for wet process of dust removal in spiral plate exchanger with axial-cross flow

XU Qipeng, GUI Yueming, ZHU Jiahua, CHENG Yuangui, XIA Sulan   

  1. School of Chemical Engineering, Sichuan University, Chengdu 610065, Sichuan, China
  • Received:2013-04-15 Revised:2013-06-03 Online:2014-02-05 Published:2014-02-05
  • Supported by:

    supported by the National Natural Science Foundation of China (21276161) and the Central University Fundamentals Research Plan (2010SCU22008).

摘要: 提出了螺旋板换热器轴向错流通道冷却冷凝湿法除尘的方法,指出了PM2.5在尾气对流传热传质边界层内热泳和伴随水蒸气冷凝的扩散泳运动特征和冷凝液膜吸收除尘机理并建立了拟均相模型,获得了PM2.5浓度衰减函数和以冷凝通量nw为参数的捕尘效率模型。通过“三传”类比获得了从尾气流速求取模型参数的方法,并通过恒壁温条件下冷却冷凝实验数据验证了模型参数计算方法的正确性,结果表明水蒸气组分扩散体积通量即PM2.5扩散泳速度Vw是控制性参数,其值在20~40 mm·s-1范围。

关键词: 螺旋板换热器, 轴向错流, 冷却冷凝, 湿法除尘, 拟均相模型

Abstract: A wet process of PM2.5 removal from industrial waste gases was proposed, with cooling and condensation in the axial channel of a spiral plate exchanger. The characteristics of thermo-phoresis and diffusion-phoresis of PM2.5 with vapor component in the boundary layer of heat and mass transfer were pointed out. A pseudo-homogeneous model was built based on the mechanism on dust removal by condensate film absorption. Subsequently, the attenuation function of PM2.5 concentration was deduced. The dust removal efficiency equation, with the condensate flux nw and the waste gas inlet velocity u0 as the variables, was obtained. Parameters in the model were derived by means of analogies of momentum, heat and mass transfer, and verified with the experimental data of cooling and condensation under constant wall temperatures. It is shown that the key factor is the vapor diffusion volume flux (or called PM2.5 diffusion-phoresis velocity) Vw with the magnitude of 20—40 mm·s-1.

Key words: spiral plate exchanger, axial-cross flow, cooling and condensation, wet dust removal, pseudo-homogeneous model

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