未修正）锅炉热效率计算成果表（未修正）序号123456789101112131415161718192021222324名主汽流量主汽压力主汽温度给水压力给水温度汽包压力设计冷风温度保证的进风温度(设计值)设计给水温度机组电负荷主蒸汽流量主蒸汽压力主蒸汽温度再热蒸汽压力再热蒸汽温度汽包压力给水压力给水温度燃料消耗量雾化用蒸汽量雾化蒸汽在入口参数下的焓基准温度下饱和汽的焓暖风器系数1(投用暖风器为1,不投暖风器为0)暖风器系数2(投用暖风器为0,不投暖风器为1)称符号DePgretgrePgsetgsePqbetnf,ck,bt0btgsb工况一锅炉额定参数935.0017.20540.00\269.0018.2020.0020.00269.00实际运行参数280.3305664850.560852116.31538.783.13536.7616.3117.06262.25100.92工况二935.0017.20540.00\269.0018.2020.0020.00269.00253.0263214767.27252215.55538.062.85535.4515.5517.28257.2391.09工况三935.0017.20540.00\269.0018.2020.0020.00269.00299.9775391921.950378416.27537.213.39539.0716.2717.89266.58107.99工况四935.0017.20540.00\269.0018.2020.0020.00269.00299.8848267916.899841316.19537.373.41535.6916.1918.01266.47107.96DPgrtgrPzrtzrPqbPgstgsBDwhhwh（hbq）0Knf,1Knf,20.000.000.000.001.00煤质分析数据0.000.000.000.001.000.000.000.000.001.000.000.000.000.001.00未修正）锅炉热效率计算成果表（未修正）序号252627282930313233343536373839404142434445464748名收到基碳收到基氢收到基硫收到基氧收到基氮收到基灰分收到基水分空干基水分干燥无灰基挥发分煤的干燥基灰分燃料温度灰的温度收到基低位发热量空干基高位发热量飞灰含碳量大渣含碳量沉降灰含碳量漏煤含碳量送风机入口风温空气预热器进口空气温度(考虑投用暖风器)实测排烟温度省煤器进口烟气实测温度（如双级交错布置时为低温级省煤器）省煤器出口烟气实测温度（如双级交错布置时为低温级省煤器）排烟RO2含量称符号CarHarSarOarNarAarMarMadVdafAdtrthQnet,arQgr,adCfh.cClz.cCcjh.cClm.ct0tky,rktpytsm,rktsm,ckRO2工况一52.463.003.234.050.7432.324.202.0828.3533.0310.0010.0020320.00实际测试分析数据工况二52.463.003.234.050.7432.324.202.0828.3533.0310.0010.0020320.00工况三52.463.003.234.050.7432.324.202.0828.3533.0310.0010.0020320.00工况四52.463.003.234.050.7432.324.202.0828.3533.0310.0010.0020320.001.130.170.000.0031.421.070.10.000.0034.531.520.140.000.0034.941.390.140.000.0033.76147.79430.22392.71157.76425.66387.24154.81436.41401.86154.70435.19402.8513.0012.3013.5014.00未修正）锅炉热效率计算成果表（未修正）序号4950515253545556575859606162636465666768697071名称排烟O2含量排烟N2含量排烟CO含量排烟CH4含量排烟H2含量排烟CmHm含量空气相对湿度中速磨煤机废弃的石子煤量石子煤低位发热量大气压力空气预热器入口实测平均烟温（如为双级交错布置时则为低温级空气预热器）空气预热器进口实测空气温度（如为双级交错布置则为低温级空气预热器）飞灰分额大渣分额沉降灰分额漏煤份额炉渣温度沉降灰温度CO2比热O2比热N2比热CO比热水蒸气平均定压比热符号O2N2COCH4H2C