t循环流化床锅炉设计计算表

烟温θ''F21分离器出口烟焓I''p36分离器数量n37汽冷旋风分离器出口烟温θ''F38误差39烟气放热量cp40分离器出口循环灰焓I''FZ41循环灰放热量Qez42总放热量Qe43工质流量Dd44蒸汽焓增Δi45蒸汽进口焓i'46蒸汽出口焓I''47蒸汽出口温度t''48蒸汽进口比容v'49蒸汽出口比容v''50平均比容vcp51蒸汽流通截面积Fn52蒸汽流速wn53蒸汽质量流速wr130t/h高温高压循环流化床1、基本数据1.1设计煤种来源数值测量值6测量值61测量值4.1测量值6.8测量值1.4测量值2.9测量值18.8测量值0测量值40测量值25140测量值0339.13*Car+1029.95Har-108.86*(Oar-Sar)-25.12*Mar24334.451|Qnet,ar-Qnet,ar校|(应小于628)805.5491.2石灰石来源数值测量值97.32测量值0测量值0.8测量值1.882、燃烧脱硫计算2.1无脱硫工况时的燃烧计算来源数值0.0889(Car+0.375Sar)+0.265Har-0.0333Oar6.379638751.866(Car+0.375Sar)/1001.158552750.79V0+0.8Nar/1005.0511146130.111Har+0.0124Mar+0.0161V00.632212184测量值0.72.3脱硫计算来源数值μ0SO2=1.998Sar*10^4/Vy6820.815195“GB13271-2001锅炉大气污染物排放标准”900(1-μSO2/μ0SO2)*10086.80509625测量值80.8测量值0.8055m=-ln((100-ηSO2j)/A)/K2.249716065见1.297.32Bd=3.122m*Sar/ηCaCO30.209293869测量值(若无,推荐15%)15