烟气焓温
表
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(kJ/Nm3)烟气流量Nm3/h14467高低温烟气焓差kJ/Nm368.9插值计算余热锅炉效率-0.95X1100135.4回收烟气热量kw263.002X5066.5回收烟气热量kJ/h946806X2200273.2容积比温度顺序理论烟气的焓ro2比例N2比例H2O比例O2比例飞灰比例ro2(℃)1100135.396.772.8114.056.440170.032200273.17357.463300414.09558.814400558.54771.885500706.63994.356600857.111224.6677001013.901461.8888001172.661704.8899001334.061952.281010001498.182203.51111001664.672458.391212001833.282716.561313002004.202976.741414002176.183239.041515002349.963503.11616002525.133768.81717002702.094036.311818002879.294304.71919003057.784574.062020003237.014844.22121003417.925115.392222003598.565386.48氮气72.81Y1二氧化碳6.7Y氧气6.44Y2水蒸汽14.05N2H2OO2飞灰空气129.5815113280.8132.43259.92304267169.1266.36392.01463407263.7402.69526.52626551360541.76663.8795699458.5684.15804.12969830559.8829.74947.5211491004663.2978.321093.613341160767.21129.121241.5515261318873.91282.321391.7172314789841437.31543.741925163810961594.891697.162132180112061753.441852.762344196413601914.252008.722559212815712076.221662779229417582238.92324.483002246018302402.882484.043229262920662567.342643.663458279721842731.862804.213690296723852898.8329653926313825123065.63127.534163330926403233.793289.224402348327603401.64