化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
2期
430-436
,共7页
徐其鹏%桂月明%朱家骅%程远贵%夏素兰
徐其鵬%桂月明%硃傢驊%程遠貴%夏素蘭
서기붕%계월명%주가화%정원귀%하소란
螺旋板换热器%轴向错流%冷却冷凝%湿法除尘%拟均相模型
螺鏇闆換熱器%軸嚮錯流%冷卻冷凝%濕法除塵%擬均相模型
라선판환열기%축향착류%냉각냉응%습법제진%의균상모형
spiral plate exchanger%axial-cross flow%cooling and condensation%wet dust removal%pseudo-homogeneous model
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。
提齣瞭螺鏇闆換熱器軸嚮錯流通道冷卻冷凝濕法除塵的方法,指齣瞭 PM2.5在尾氣對流傳熱傳質邊界層內熱泳和伴隨水蒸氣冷凝的擴散泳運動特徵和冷凝液膜吸收除塵機理併建立瞭擬均相模型,穫得瞭 PM2.5濃度衰減函數和以冷凝通量nw為參數的捕塵效率模型。通過“三傳”類比穫得瞭從尾氣流速求取模型參數的方法,併通過恆壁溫條件下冷卻冷凝實驗數據驗證瞭模型參數計算方法的正確性,結果錶明水蒸氣組分擴散體積通量即 PM2.5擴散泳速度Vw是控製性參數,其值在20~40 mm·s-1範圍。
제출료라선판환열기축향착류통도냉각냉응습법제진적방법,지출료 PM2.5재미기대류전열전질변계층내열영화반수수증기냉응적확산영운동특정화냉응액막흡수제진궤리병건립료의균상모형,획득료 PM2.5농도쇠감함수화이냉응통량nw위삼수적포진효솔모형。통과“삼전”류비획득료종미기류속구취모형삼수적방법,병통과항벽온조건하냉각냉응실험수거험증료모형삼수계산방법적정학성,결과표명수증기조분확산체적통량즉 PM2.5확산영속도Vw시공제성삼수,기치재20~40 mm·s-1범위。
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.