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新金瓶梅之2奴爱

类型:92全能午夜手机福利免费视频 地区: 新加披 年份:2020-07-02

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热段冷段1管径及壁厚d×δ㎜φ60×7φ42×3.5φ38×4φ32×4波形板波形板2计算受热面积A ㎡6241275040204622919095220864523烟气进口温度θ'ds ℃#NAME?#NAME?#NAME?#NAME?390#NAME?4烟气出口温度θ"ds ℃#NAME?#NAME?#NAME?390#NAME?#NAME?5工质进口温度t'ds ℃—#NAME?—24053206工质出口温度t"ds ℃—#NAME?—#NAME?354537烟气流速w y m/s —#NAME?—#NAME?#NAME?#NAME?8工质流速w m/s —#NAME?— 1.3#NAME?#NAME?9传热温差Δt℃—#NAME?######NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?10热有效或利用系数0.45————0.65—0.650.800.6011传热系数k w/(㎡·℃)—#NAME?######NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?12吸热量/附加吸热量Q xr /Q fj kJ/kg #NAME?#NAME?176#####252#NAME?150180604721713736#NAME?124#NAME?81#NAME?#NAME?#NAME?13焓增量Δh kJ/kg —#NAME?—#NAME?#NAME?#NAME?14喷水量D jw kJ/kg ————————————15烟气旁通量份额δ——0.1500.150———#NAME?85.00.65低再引出管第三转向室主省煤器低温再热器1.1#NAME?—旁路省煤器φ38×4530#NAME?#NAME?#NAME?#NAME?#NAME?—#NAME?#NAME?#NAME?#NAME?#NAME?0.60—#NAME?——————φ38×4#NAME?φ42×3.55630#NAME?#NAME?324#NAME?#NAME?#NAME?#NAME?#NAME?φ38×4706——#NAME?——— 6.50E+03540#NAME?#NAME?#NAME?#NAME?#NAME?0.65φ38×5519φ38×6#NAME?—#NAME?1006#NAME?#NAME?—炉 膛第一转向室第二转向室空气预热器1200前 屏对流过热器φ38×4.5288后 屏1006—#NAME?#NAME? 热 力 计 算 结 果 汇 总 表序 号名 称符 号单 位数 值5.50E+03#NAME?540#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?——#NAME?0.3470.00700.65706#NAME?高温再热器φ42×4.51177#NAME?—0.7100.7100.29————

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