课程设计表格lkjsdflk

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1、一．辅助计算燃烧计算表序号项目名称符号单位（标况）计算公式及数据结果1理论空气量2理论氮容量3RO2容积4理论干烟气容积5理论水蒸气容积6飞灰份额烟气特性表序号项目名称符号单位炉膛屏凝渣管高过低过高温省煤器高温空预器低温省煤器低温空预器1受热面出口过量空气系数2烟道平均过量空气系数3干烟气容积4水蒸气容积5烟气总容积6RO2容积份额7水蒸气容积份额8三原子气体和水蒸汽容积总份额9容积飞灰浓度10烟气质量11质量飞灰浓度烟气焓温表（炉膛，屏式过热器，高温过热器）烟气或空气温度理论烟气焓理论空气焓理论烟气焓增炉膛，屏，凝渣管高温过热器4002663.933673.647984.740

2、83740.2451002.1895003986.01583361.86845.154764658.3882137.0214742.4342176.2596005809.136464931.3621823.120666795.4091235.4686918.6931257.4517006868.738885810.68921059.602428030.8771263.0318176.1441285.4598007952.339186707.84061083.60039293.9071284.7219461.6031307.4479009055.253587616.87481102

3、.914410578.631309.00610769.051332.029100010180.07658537.79181124.8229211887.631324.91312101.081348.382110011317.241449476.5331137.1649413212.551336.83913449.461360.308120012466.3326610415.27421149.0912214549.391354.93514809.771378.849130013629.9543411371.83961163.6216815904.321366.81316188.62

4、1390.875140014804.2657412334.34641174.311417271.141382.15817579.491406.37150015992.734513302.79461188.4687618653.291386.69118985.861411.051160017184.547814277.18421191.813320039.981402.27720396.911426.637170018391.946915251.57381207.399121442.261404.95621823.551429.464180019600.836616231.9048

5、1208.889722847.221411.723253.021436.506190020814.094217224.11861213.257624258.921417.45124689.521442.108200022034.29118210.3911220.196825676.371429.02126131.631454.124210023262.49319214.48761228.20227105.391427.3927585.751452.195220024491.440320206.70141228.947328532.781427.3929037.951452.195

6、烟气焓温表（低温过热器，高温省煤器）烟气或空气温度理论烟气焓理论空气焓理论烟气焓增低温过热器高温过热器3002784.66152388.44283369.833417.5994003763.44563220.2388978.78414552.4041182.5744616.8091199.215004775.10874063.91761011.66315770.7691218.3645852.0471235.2386005809.49894931.3621034.39027017.6831246.9147116.311264.2637006868.86685810.6892105

7、9.36798292.4861274.8038408.6991292.398007952.46716707.84061083.60039595.8881303.4029730.0451321.345烟气焓温表（高温空预器，低温省煤器）烟气或空气温度理论烟气焓理论空气焓理论烟气焓增高温空预器低温省煤器100899.7407784.26481146.7841162.4692001829.99121580.4124930.25052327.8211181.0372359.4291196