首页> 外文会议>Conference on engineering papermakers : Forming bonds for better papermaking >DEVELOPMENT OF A RECOVERY BOILER LOWER FURNACE HEAT TRANSFER MODEL - PART I: ANALYSIS OF FLOOR TUBE TEMPERATURE EXCURSIONS
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DEVELOPMENT OF A RECOVERY BOILER LOWER FURNACE HEAT TRANSFER MODEL - PART I: ANALYSIS OF FLOOR TUBE TEMPERATURE EXCURSIONS

机译:回热锅炉下部炉膛传热模型的开发-第一部分:炉内温度波动的分析

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An advanced heat transfer model, using the PHOENICS code as a base, has been developed to simulate heat transfer in the lower furnace of kraft recovery boilers. Simulation results show that the heat transfer regime inside a floor tube can be either forced convection, flow boiling, combined convection/boiling or post-critical heat flux (CHF), depending on the thickness of the frozen smelt on the tube. Under steady-state conditions, high tube temperature excursions may occur only when flow inside the tube is slow and the molten smelt flow is rapid. Under transient conditions where the frozen smelt layer cracks and molten smelt comes into contact with the floor tube, the outer tube surface temperature can increase significantly.
机译:已经开发了一种先进的传热模型,该模型以PHOENICS代码为基础,用于模拟牛皮纸回收锅炉下部炉膛中的传热。仿真结果表明,取决于管上的冰冻熔体的厚度,地板管内部的传热方式可以是强制对流,流动沸腾,组合对流/沸腾或临界后热通量(CHF)。在稳态条件下,仅当管内流动缓慢且熔融熔体流动迅速时,才可能发生高管温偏移。在瞬态条件下,冻结的熔体层破裂并且熔化的熔体与地板管接触,外管表面温度会显着升高。

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