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吸收器外侧边界层系数Q3293αo347.1722059~1300~待求ξm0.617混合浓度3829027.23蒸发冷凝tsd5.5t26.46管壁温度膜内分压饱和tss-12.9992596手动查取Pss558.00~600~没有用-1.181163874K301tsd-tss18.4992596太大，应小于18.35αi9446.95水导热系数0.608030681349.9961178-12.9992596公式准2.5动力粘度0.000898184-358.9383921公式不准22.5密度996.15T混46.227.8水出Q/A6422.428762已知27.8运动粘度9.01655E-07稀40.822.5水进水平均温度25.15比容4177.5043.525.15管子内径16管内雷诺数44362.8818.35A596.1961388已知污垢热阻0.00009管内普朗特数6.171890023002300.618090.0268734781890023002300.810730.035249137949.33043654.9225678631.23553353.6167686797949.33043654.9225678602.41026738.0180929837357.418391479.7033662520.01941998.4043716527357.418391479.7033662494.98210013.1850378856926.085966441.1124943437.61967560.7918203866926.085966441.1124943415.68869665.7635632596507.776652360.7250373356.61633261.139012916507.776652360.7250373337.97654926.3063235826422.428762347.1722059339.95716362.0782315436422.428762347.1722059322.02258597.2441340582.6761797755.0920668168.4043716528.0180929831890023002300.810730.035249137483.056532630.8799615517.918578317.905368717949.33043654.9225678602.41026738.0180929837357.418391479.7033662494.98210013.1850378856926.085966441.1124943415.68869665.7635632597388.173863370.9908095500.603487834.936897367168.001887365.8686683460.265774425.800817146507.776652360.7250373337.97654926.3063235826422.428762347.1722059322.02258597.24413405812.13283157
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