![](https://img62.hbzhan.com/5eceadd4559dcfd2f25b3d782573a1c04df22fa7dadb702a85eee941c41eaea424530ae0285663bb.jpg) 导热油炉余热回收节能效益分析 Analysis of Energy-saving Effect for Waste Heat Revovery of HTM Heating Boiler 导热油炉规格(万大卡/时) | 120 | 200 | 300 | 400 | 600 | 800 | 1000 | 1200 | 导热油炉排烟温度(℃) | 350 | 350 | 350 | 350 | 350 | 350 | 350 | 350 | 导热油炉排烟量(Nm3/h) | 2800 | 4600 | 7000 | 9300 | 14000 | 19000 | 23000 | 28000 | 余热锅炉蒸汽压力(Mpa) | 0.6 | 0.6 | 0.6 | 0.6 | 0.6 | 0.6 | 0.6 | 0.6 | 余热锅炉蒸汽产量(t/h) | 0.27 | 0.44 | 0.65 | 0.87 | 1.34 | 1.83 | 2.23 | 2.73 | 配用余热锅炉 | 0.3 | 0.5 | 0.8 | 1 | 1.5 | 2.0 | 2.5 | 3.0 | 除尘器前烟气温度(℃) | 152 | 150 | 150 | 149 | 146 | 149 | 149 | 147 | 年产蒸汽量(t) | 1944 | 3168 | 4680 | 6264 | 9648 | 13176 | 16056 | 19656 | 年经济效益(万元) | 38.9 | 63.3 | 93.6 | 125.3 | 193 | 263.5 | 321.1 | 393.1 | 说明:由于产品在更新进步,所以上表中数据供参考,实际数据在技术、商务洽谈中予以明确。 说明:表中蒸汽按200元/吨计算,每年按7200小时生产计算。 表中计算还需根据导热油炉实际使用工作况进行修正。 Note: The vapor shown in the table is accordance with ¥200/ton and the the total required volume can be calculated according to 7200 hour-production The calculations shown in the table shall be modified in accordance with the working condition of actual use in HTM boiler.
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