序号项 目符号计算公式或依据单位数据数据数据数据一垃圾元素分析值设计值校核高值(风机选型）校核低值设计值1应用基碳Car垃圾元素分析％16.80018.70016.80017.0002应用基氢Har垃圾元素分析％1.8002.4001.0002.2003应用基氧Oar垃圾元素分析％12.78012.78012.78012.7804应用基氮Nar垃圾元素分析％0.4000.4000.4000.4005应用基硫Sar垃圾元素分析％0.1400.1400.1400.1406应用基氯Clar垃圾元素分析％0.3480.3480.3480.3487应用基水份Mar垃圾元素分析％45.00045.00045.50045.0008应用基灰份Aar垃圾元素分析％22.73220.23223.03222.132合计100.000100.000100.000100.00010收到基低位发热量Qnet,arQnet,ar=339Car+1030Har-109(Oar-Sar)-MarkJ/kg5046.446308.544209.945526.24kcal/kg1205.551507.061005.721320.17二垃圾量计算（一）天垃圾焚烧量Wd工程设计值t/d1000.001000.001000.001000.001垃圾焚烧炉台数z工程设计值台2.002.002.002.002设计每小时垃圾焚烧量 t/hBj单台焚烧炉工程设计值 Wd/24/zt/h20.8320.8320.8320.833设计每小时最大垃圾焚烧量Bjz1.1*Bjt/h22.9222.9222.9222.92三燃烧计算1NOX转化率0.0500.0500.0500.0502SOX的转化率0.6000.6000.6000.6003理论干空气量V00.0889(Car+0.375Sar)+0.265Har+0.008*N转化率Nar-0.0333OarNm3/kg1.5501.8781.3381.6744理论湿空气量Vw01.016V0Nm3/kg1.5751.9081.3591.7005炉膛出口过量空气系数α传统焚烧炉排取值范围1.6～1.8（新型燃烧技术为1.3～1.4）氧含量7-9%1.7001.7001.7001.7006实际干空气量V0aα*V0Nm3/kg2.6353.1922.2742.8457实际湿空气量Va.w01.016*α*V0Nm3/kg2.6773.2432.3112.891含氧量8.6478.6478.6478.647垃圾焚烧发电设计计算完整版（锅炉蒸发量、烟气量、发电量、风机选型等）第1页 共126页（二）燃烧产物理论体积1氮容积V0N20.79*V0+0.008*(1-N转化率)*NarNm3/kg1.22741.48641.05991.32512三原子气体容积V0RO21.866(Car+0.375*S转*Sar)/100Nm3/kg0.31410.34950.31410.3178其中SO2V0SO21.866*0.375*S转*Sar/100Nm3/kg0.00060.00060.00060.0006其中CO2V0CO21.866*Car/100Nm3/kg0.31350.34890.31350.31723NOV0NO0.016*β*NarNm3/kg0.00030.00030.00030.00034水蒸气V0H2O0.111Har-0.00315Clar+0.0124Mar+0.0161*V0Nm3/kg0.78350.85590.69660.83025燃烧产物理论干烟气体积（干烟气）V0dgV0N2+V0RO2+V0NO+V0HCLNm3/kg1.54401.83851.37651.64556燃烧产物理论湿烟气体积(湿烟气)V0wyV0N2+V0R...
