垃圾发电计算表格表格文件下载.xls

垃圾发电计算表格表格文件下载.xls

《垃圾发电计算表格表格文件下载.xls》由会员分享，可在线阅读，更多相关《垃圾发电计算表格表格文件下载.xls（13页珍藏版）》请在冰豆网上搜索。

垃垃圾圾焚焚烧烧计计算算序号项目符号计算公式或依据单位数据数据数据数据一一垃垃圾圾元元素素分分析析值值设计值校核高值（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/kg1205.551507.061005.721320.17二二垃垃圾圾量量计计算算（一一）天天垃垃圾圾焚焚烧烧量量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/h22.9222.9222.9222.92三三燃燃烧烧计计算算1NOXNOX转转化化率率0.0500.0500.0500.0502SOXSOX的的转转化化率率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传统焚烧炉排取值范围1.61.8（新型燃烧技术为1.31.4）氧含量7-9%1.7001.7001.7001.7006实际干空气量V0a*V0Nm3/kg2.6353.1922.2742.8457实际湿空气量Va.w01.016*V0Nm3/kg2.6773.2432.3112.891含氧量8.6478.6478.6478.647第1页共13页

（二）燃燃烧烧产产物物理理论论体体积积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*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+V0RO2+V0H2O+V0NO+V0HCLNm3/kg2.32742.69442.07312.47577实际燃烧产体积（干烟气）VdgV0dg+（-1）*V0Nm3/kg2.62883.15282.31292.81708实际水蒸汽容积VH2OV0H2O+0.016*（-1）*V0Nm3/kg0.80080.87700.71160.84909实际燃烧产体积（湿烟气）Va.wgVdg+VH2ONm3/kg3.42964.02983.02453.665910HCL含量估算V0HCL0.631*Clar/100Nm3/kg0.00220.00220.00220.0022（三）燃燃烧烧产产物物实实际际体体积积1当地大气压PdMPa0.100.100.100.102气压修正系数Mp0.101325/PdMPa1.001.001.001.00一焚焚烧烧炉炉出出口口烟烟气气量量1炉排漏风系数py1不计入炉膛出口过剩空气计算0.020.020.020.022炉膛漏风系数py2不计入炉膛出口过剩空气计算0.020.020.020.023炉膛出口烟气温度TGT850.00850.00850.00850.004炉膛出口燃烧产物的体积（标态、湿烟气）VpydwVa.wgNm3/kg3.434.033.023.675炉膛出口烟气量（标态、湿烟气）Qpy1000*Bjz*VpydwNm3/h78595.1592349.5469312.3584011.356炉膛出口烟气量（实际、湿烟气）Vpy1Mp*Qpy*（273+TGT）/273m3/h324281.44381031.70285980.86346628.547炉膛出口燃烧产物的实际体积（干烟气）VpydgVdgNm3/kg2.633.152.312.828炉膛出口烟气量（标态、干烟气）Qpg1000*Bjz*VpydgNm3/h60243.1972252.4453004.2764555.299炉膛出口烟气量（实际、干烟气）Vpy2Mp*Qpg*（273+TGT）/273m3/h248561.77298111.60218694.19266353.36二余余热热炉炉出出口口烟烟气气量量1余热锅炉漏风系数py30.030.030.030.032余热锅炉出口烟气温度TYT220.00220.00220.00220.00第2页共13页3余热锅炉出口燃烧产物的体积（标态、湿烟气）VrydwVpydw+1.016*py3*V0Nm3/kg3.484.093.073.724余热锅炉出口烟气量（标态、湿烟气）Vry11000*Bjz*VrydwNm3/h79677.6693661.1170246.7885180.335余热锅炉出口烟气量（实际、湿烟气）QrydwMp*Vry1*（273+TYT）/273m3/h144321.19169649.58127238.92154288.246余热锅炉出口燃烧产物的实际体积（干烟气）VrydgVpydg*py3*V0Nm3/kg2.683.212.352.877余热锅炉出口烟气量（标态、干烟气）Vry21000*Bjz*VrydgNm3/h61308.6673543.3553923.9965705.868余热锅炉出口烟气量（实际、干烟气）Qrydg1000*Bjz*Mp*Vry2*（273+TYT）/273m3/h111049.18133210.0297673.23119013.87除除尘尘器器出出口口烟烟气气量量1除尘器漏风系数py40.200.200.200.202除尘器出口烟气温度TYT150.00150.00150.00150.003除尘器出口燃烧产物的体积（标态、湿烟气）VrydwVpydw+1.016*py4*V0Nm3/kg3.794.473.344.064除尘器出口烟气量（标态、湿烟气）Vry11000*Bjz*VrydwNm3/h86894.44102404.8576476.3592973.515除尘器出口烟气量（实际、湿烟气）QrydwMp*Vry1*（273+TYT）/273m3/h135045.14159150.31118854.08144492.796除尘器出口燃烧产物的实际体积（干烟气）VrydgVpydg+py4*V0Nm3/kg2.943.532.583.157除尘器出口烟气量（标态、干烟气）Vry21000*Bjz*VrydgNm3/h67346.3280858.4959135.7472225.748除尘器出口烟气量（实际、干烟气）Qrydg1000*Bjz*Mp*Vry2*（273+TYT）/273m3/h104664.84125664.4991904.54112248.09三组组分分分分析析一一（实实际际氧氧，湿湿态态，标标态态）体体积积浓浓度度1氮含量（实际氧，湿态，标态）N2（V0N2+0.79*（+py3-1）*V0）/Vrydw%61.006962.864059.745161.61722二氧化硫（实际氧，湿态，标态）SO2V0SO2/Vrydw%0.01690.01440.01920.01583二氧化碳（实际氧，湿态，标态）CO2V0C02/Vrydw%9.01658.537810.22698.53444一氧化氮（实际氧，湿态，标态）NOV0N0/Vrydw（未脱硝）%0.00920.00780.01040.00865水汽容积（实际氧，湿态，标态）H2O（V0H2O+0.0161*（+py3-1）*V0）/Vrydw%23.057421.482723.239522.86596氧含量（实际氧，湿态，标态）O2（0.21*（+py3-1）*V0）/Vrydw%6.83327.04306.69046.90237氯化氢（实际氧，湿态，标态）HCLV0HCL/Vrydw%0.06320.05370.07160.0591四组分分析二（实际氧，湿态，标态）质量浓度1二氧化硫（实际氧，湿态，标态）SO2E78/22.4*64*10000mg/Nm3483.0243410.9096547.8721451.82092氯化氢（实际氧，湿态，标态）HCLE83/22.4*36*10000mg/Nm31015.0278863.48591151.2989949.45683氮氧化物（实际氧，湿态，标态）以NO2计E80/22.4*46*10000mg/Nm3189.0056160.7874214.3803176.7958第3页共13页五组分分析三（实际氧，干态，标态）质量浓度1二氧化硫（实际氧，干态，标态）SO2（E33/E62*100）/22.4*64*10000mg/Nm3627.7457523.3138713.7129585.73552氯化氢（实际氧，干态，标态）HCL（E42/E62*100）/22.4*36*10000mg/Nm31319.14551099.69221499.79701230.86513氮氧化物（实际氧，干态，标态）以NO2计（E35/E62*100）/22.4*46*10000mg/Nm3245.6345204.7707279.2732229.1961六（11%O2，干态，标态）质量浓度及达标计算

（一）初始排放浓度1二氧化硫（11%O2，干态，标态）SO2（E33/（E37+（1-0.0161）*（2.1-1）*E22）*100）/22.4*64*10000mg/Nm3521.3493433.8803594.6187485.83342氯化氢（11%O2，干态，标态）HCL（E42/（E37+（1-0.0161）*（2.1-1）*E22）*100）/22.4*36*10000mg/Nm31095.5640911.75641249.53231020.93073氮氧化物（11%O2，干态，标态）以NO2计（E35/（E37+（1-0.0161）*（2.1-1）*E22）*100）/22.4*46*10000mg/Nm3204.0020169.7757232.6720190.10484烟尘（11%O2，干态，标态）（1*0.04*1000）/（E37+（1-0.0161）*（2.1-